Characterization, Cleanup, and Revitalization of Mining Sites
Treatment Technologies for Mining-Influenced Water Profile
Technology: Fluidized bed reactor (FBR)
- Report
- FINAL, APPENDIX C, Phase 2 Treatability Study Report, Ultrafiltration/Reverse Osmosis and Biological Selenium Removal Fluidized Bed Bioreactor Treatment Technology
Source or source contact: Lynne Hood , Remedial Project Manager, Hood.Lynne@epa.gov, (208) 378-5757
Publication Date: February 2023
Document Type: PDF
Author: Formation Environmental
Prepared for: J.R. Simplot Company
Site Identifiers
| Site Name: | USDA FS CARIBOU-TARGHEE NF: SMOKY CANYON MINE SITE |
| EPA CERCLA ID: | IDN001002800 |
| Parent Name (if applicable): | SOUTHEAST IDAHO SELENIUM PROJECT/AKA SMOKY CANYON MINE (# IDN001002245) |
Miscellaneous Study Information
| Operable Unit (OU): | N/A |
| Sample Site ID: | LSSHS-ROC (influent) and LSSHS-BE1 (effluent from FBR #1) |
| Site Status: | Data not provided |
| Technology Tested: | Fluidized bed reactor (FBR) |
| Technology Type: | Active |
| Technology Name: | Fluidized bed reactor (FBR) |
| Pre-treatment or No Pre-treatment: | Pre-treatment |
| Source of MIW: | Groundwater springs (Hoopes Spring and South Fork Sage Creek spring) |
| Treatment Train? (Y/N): | Y |
| Specific Component for Performance Data: | FBR/part of treatment train with ultrafiltration (UF) and reverse osmosis (RO) pre-treatment |
| Technology Requirements: | Pumps to pump water from springs to treatment area. UF/RO (ultrafiltration/reverse osmosis) system to treat water prior to FBR |
| Geographic conditions/constraints: | Southeast Idaho. No constraints noted. |
| Scale: | Pilot |
| Duration of Study: | One sampling event (4/16/2016) |
Data Set #1
Constituent Information
| Constituent: | Manganese |
| Constituent Phase: | Mn, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.00187 |
| Associated Effluent/ | 0.00569 |
| % Removal Efficiency (calculated): | -204.28 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #2
Constituent Information
| Constituent: | Boron |
| Constituent Phase: | B, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.04 |
| Associated Effluent/ | 0.0409 |
| % Removal Efficiency (calculated): | -2.25 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes: Estimated quantity
Data Set #3
Constituent Information
| Constituent: | Boron |
| Constituent Phase: | B, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.0422 |
| Associated Effluent/ | 0.0417 |
| % Removal Efficiency (calculated): | 1.18 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 7 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes: Estimated quantity
Data Set #4
Constituent Information
| Constituent: | Total Dissolved Solids |
| Constituent Phase: | TDS mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
1150 |
| Associated Effluent/ | 1130 |
| % Removal Efficiency (calculated): | 1.74 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 1,134 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #5
Constituent Information
| Constituent: | Silver |
| Constituent Phase: | Ag, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
ND |
| Associated Effluent/ | ND |
| % Removal Efficiency (calculated): | Not Applicable |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 0.0034 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes: ND = non-detect
Data Set #6
Constituent Information
| Constituent: | Silver |
| Constituent Phase: | Ag, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
ND |
| Associated Effluent/ | ND |
| % Removal Efficiency (calculated): | Not Applicable |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Influent and effluent below the detection limit (0.0000172 mg/L) |
Notes: ND = non-detect
Data Set #7
Constituent Information
| Constituent: | Aluminum |
| Constituent Phase: | Al, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
ND |
| Associated Effluent/ | 0.0069 |
| % Removal Efficiency (calculated): | Not Applicable |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Influent below the detection limit (0.0076 mg/L) |
Notes: ND = non-detect
Data Set #8
Constituent Information
| Constituent: | Aluminum |
| Constituent Phase: | Al, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.0098 |
| Associated Effluent/ | ND |
| % Removal Efficiency (calculated): | 61.22 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 0.39 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Effluent below the detection limit (0.0076 mg/L) |
Notes: ND = non-detect
Data Set #9
Constituent Information
| Constituent: | Alkalinity |
| Constituent Phase: | Alkalinity as CaCO3 mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
780 |
| Associated Effluent/ | 790 |
| % Removal Efficiency (calculated): | -1.28 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #10
Constituent Information
| Constituent: | Ammonia |
| Constituent Phase: | Ammonia (as N) mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
ND |
| Associated Effluent/ | 3.9 |
| % Removal Efficiency (calculated): | Not Applicable |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Influent below the detection limit (0.026 mg/L) |
Notes: ND = non-detect
Data Set #11
Constituent Information
| Constituent: | Arsenic |
| Constituent Phase: | As, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.00142 |
| Associated Effluent/ | ND |
| % Removal Efficiency (calculated): | 85.99 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 0.01 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Effluent below the detection limit (0.000398 mg/L) |
Notes: ND = non-detect
Data Set #12
Constituent Information
| Constituent: | Arsenic |
| Constituent Phase: | As, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.00165 |
| Associated Effluent/ | 0.0006 |
| % Removal Efficiency (calculated): | 63.64 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 0.01 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #13
Constituent Information
| Constituent: | Barium |
| Constituent Phase: | Ba, Dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.203 |
| Associated Effluent/ | 0.208 |
| % Removal Efficiency (calculated): | -2.46 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #14
Constituent Information
| Constituent: | Barium |
| Constituent Phase: | Ba, Total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.211 |
| Associated Effluent/ | 0.211 |
| % Removal Efficiency (calculated): | 0.00 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 0.44 |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #15
Constituent Information
| Constituent: | Beryllium |
| Constituent Phase: | Be, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
ND |
| Associated Effluent/ | ND |
| % Removal Efficiency (calculated): | Not Applicable |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Influent and effluent below the detection limit (0.000047 mg/L) |
Notes: ND = non-detect
Data Set #16
Constituent Information
| Constituent: | Beryllium |
| Constituent Phase: | Be, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
ND |
| Associated Effluent/ | ND |
| % Removal Efficiency (calculated): | Not Applicable |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 0.0067 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Influent and effluent below the detection limit (0.000047 mg/L) |
Notes: ND = non-detect
Data Set #17
Constituent Information
| Constituent: | BOD |
| Constituent Phase: | Biochemical Oxygen Demand mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
ND |
| Associated Effluent/ | 28 |
| % Removal Efficiency (calculated): | Not Applicable |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Influent below the detection limit (2 mg/L) |
Notes: ND = non-detect
Data Set #18
Constituent Information
| Constituent: | Calcium |
| Constituent Phase: | Ca, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
244 |
| Associated Effluent/ | 245 |
| % Removal Efficiency (calculated): | -0.41 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #19
Constituent Information
| Constituent: | Cadmium |
| Constituent Phase: | Cd, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
ND |
| Associated Effluent/ | ND |
| % Removal Efficiency (calculated): | Not Applicable |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 0.005 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Influent and effluent below the detection limit (0.0000362 mg/L) |
Notes: ND = non-detect
Data Set #20
Constituent Information
| Constituent: | Cadmium |
| Constituent Phase: | Cd, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
6.54e-05 |
| Associated Effluent/ | ND |
| % Removal Efficiency (calculated): | 72.32 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 0.005 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Effluent below the detection limit (0.0000362 mg/L) |
Notes: ND = non-detect, estimated quantity
Data Set #21
Constituent Information
| Constituent: | Chloride |
| Constituent Phase: | Cl mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
38.3 |
| Associated Effluent/ | 38.1 |
| % Removal Efficiency (calculated): | 0.52 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #22
Constituent Information
| Constituent: | Cobalt |
| Constituent Phase: | Co, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.000319 |
| Associated Effluent/ | 0.00814 |
| % Removal Efficiency (calculated): | -2451.72 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #23
Constituent Information
| Constituent: | Cobalt |
| Constituent Phase: | Co, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.000315 |
| Associated Effluent/ | 0.00742 |
| % Removal Efficiency (calculated): | -2255.56 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 0.1 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #24
Constituent Information
| Constituent: | COD |
| Constituent Phase: | Chemical Oxygen Demand mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
ND |
| Associated Effluent/ | 5 |
| % Removal Efficiency (calculated): | Not Applicable |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Influent below the detection limit (5 mg/L) |
Notes: ND = non-detect
Data Set #25
Constituent Information
| Constituent: | Chromium |
| Constituent Phase: | Cr, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.00236 |
| Associated Effluent/ | 0.0016 |
| % Removal Efficiency (calculated): | 32.20 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 0.074 mg/L (Cr III); 0.011 mg/L (Cr VI) |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #26
Constituent Information
| Constituent: | Chromium |
| Constituent Phase: | Cr, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.0029 |
| Associated Effluent/ | 0.00172 |
| % Removal Efficiency (calculated): | 40.69 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #27
Constituent Information
| Constituent: | Copper |
| Constituent Phase: | Cu, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.000188 |
| Associated Effluent/ | 0.000324 |
| % Removal Efficiency (calculated): | -72.34 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 0.011 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes: Estimated quantity
Data Set #28
Constituent Information
| Constituent: | Copper |
| Constituent Phase: | Cu, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.000925 |
| Associated Effluent/ | 0.00172 |
| % Removal Efficiency (calculated): | -85.95 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes: Influent estimated quantity
Data Set #29
Constituent Information
| Constituent: | Fluoride |
| Constituent Phase: | F mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.464 |
| Associated Effluent/ | 1.53 |
| % Removal Efficiency (calculated): | -229.74 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #30
Constituent Information
| Constituent: | Iron |
| Constituent Phase: | Fe, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
ND |
| Associated Effluent/ | ND |
| % Removal Efficiency (calculated): | Not Applicable |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Influent and effluent below the detection limit (0.01 mg/L) |
Notes: ND = non-detect
Data Set #31
Constituent Information
| Constituent: | Iron |
| Constituent Phase: | Fe, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.0875 |
| Associated Effluent/ | 0.0356 |
| % Removal Efficiency (calculated): | 59.31 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 1 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #32
Constituent Information
| Constituent: | Hardness |
| Constituent Phase: | Hardness mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
983 |
| Associated Effluent/ | 1010 |
| % Removal Efficiency (calculated): | -2.75 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #33
Constituent Information
| Constituent: | Mercury |
| Constituent Phase: | Hg, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
6.3e-05 |
| Associated Effluent/ | 5.9e-05 |
| % Removal Efficiency (calculated): | 6.35 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 0.00077 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #34
Constituent Information
| Constituent: | Mercury |
| Constituent Phase: | Hg, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
5.2e-05 |
| Associated Effluent/ | 5.7e-05 |
| % Removal Efficiency (calculated): | -9.62 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #35
Constituent Information
| Constituent: | Potassium |
| Constituent Phase: | K, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
3.44 |
| Associated Effluent/ | 3.34 |
| % Removal Efficiency (calculated): | 2.91 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #36
Constituent Information
| Constituent: | Magnesium |
| Constituent Phase: | Mg, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
92.9 |
| Associated Effluent/ | 93.4 |
| % Removal Efficiency (calculated): | -0.54 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #37
Constituent Information
| Constituent: | Manganese |
| Constituent Phase: | Mn, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.00166 |
| Associated Effluent/ | 0.00552 |
| % Removal Efficiency (calculated): | -232.53 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 1.65 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #38
Constituent Information
| Constituent: | Molybdenum |
| Constituent Phase: | Mo, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.0043 |
| Associated Effluent/ | 0.00519 |
| % Removal Efficiency (calculated): | -20.70 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #39
Constituent Information
| Constituent: | Molybdenum |
| Constituent Phase: | Mo, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.00395 |
| Associated Effluent/ | 0.00537 |
| % Removal Efficiency (calculated): | -35.95 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 3.2 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #40
Constituent Information
| Constituent: | Sodium |
| Constituent Phase: | Na, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
29.4 |
| Associated Effluent/ | 29.1 |
| % Removal Efficiency (calculated): | 1.02 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #41
Constituent Information
| Constituent: | Nickel |
| Constituent Phase: | Ni, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.00108 |
| Associated Effluent/ | 0.0077 |
| % Removal Efficiency (calculated): | -612.96 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 0.052 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #42
Constituent Information
| Constituent: | Nickel |
| Constituent Phase: | Ni, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
ND |
| Associated Effluent/ | 0.00776 |
| % Removal Efficiency (calculated): | Not Applicable |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Influent below the detection limit (0.0000533 mg/L) |
Notes: ND = non-detect
Data Set #43
Constituent Information
| Constituent: | Nitrate |
| Constituent Phase: | as N (NO3) mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
1.23 |
| Associated Effluent/ | 0.28 |
| % Removal Efficiency (calculated): | 77.24 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #44
Constituent Information
| Constituent: | Nitrate + Nitrite |
| Constituent Phase: | NO3 + NO2 mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
1.23 |
| Associated Effluent/ | 0.281 |
| % Removal Efficiency (calculated): | 77.15 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #45
Constituent Information
| Constituent: | Lead |
| Constituent Phase: | Pb, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
ND |
| Associated Effluent/ | ND |
| % Removal Efficiency (calculated): | Not Applicable |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 0.0025 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Influent and effluent below the detection limit (0.0000554 mg/L) |
Notes: ND = non-detect
Data Set #46
Constituent Information
| Constituent: | Lead |
| Constituent Phase: | Pb, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
ND |
| Associated Effluent/ | ND |
| % Removal Efficiency (calculated): | Not Applicable |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Influent and effluent below the detection limit (0.0000554 mg/L) |
Notes: ND = non-detect
Data Set #47
Constituent Information
| Constituent: | Antimony |
| Constituent Phase: | Sb, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
8.09e-05 |
| Associated Effluent/ | 7.45e-05 |
| % Removal Efficiency (calculated): | 7.91 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #48
Constituent Information
| Constituent: | Antimony |
| Constituent Phase: | Sb, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
7.34e-05 |
| Associated Effluent/ | 7.32e-05 |
| % Removal Efficiency (calculated): | 0.27 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 0.24 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #49
Constituent Information
| Constituent: | Selenium |
| Constituent Phase: | Selenium, +6 (Selenate) mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.599 |
| Associated Effluent/ | 0.000157 |
| % Removal Efficiency (calculated): | 99.97 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #50
Constituent Information
| Constituent: | Selenium |
| Constituent Phase: | Selenium, +4 (Selenite) mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
ND |
| Associated Effluent/ | ND |
| % Removal Efficiency (calculated): | Not Applicable |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Influent and effluent below the detection limit (0.00005 mg/L) |
Notes: ND = non-detect
Data Set #51
Constituent Information
| Constituent: | Selenium |
| Constituent Phase: | Se, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.62 |
| Associated Effluent/ | 0.0039 |
| % Removal Efficiency (calculated): | 99.37 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #52
Constituent Information
| Constituent: | Selenium |
| Constituent Phase: | Se, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.574 |
| Associated Effluent/ | 0.0144 |
| % Removal Efficiency (calculated): | 97.49 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | 97% |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y, for this data point; N for overall system performance over a longer period did not meet with average effluent of 0.024 mg/l |
| Performance Metrics: | 0.0167 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #53
Constituent Information
| Constituent: | Vanadium |
| Constituent Phase: | V, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.00762 |
| Associated Effluent/ | 0.00735 |
| % Removal Efficiency (calculated): | 3.54 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 0.027 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #54
Constituent Information
| Constituent: | Sulfate |
| Constituent Phase: | Sulfate (SO42-) mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
219 |
| Associated Effluent/ | 229 |
| % Removal Efficiency (calculated): | -4.57 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #55
Constituent Information
| Constituent: | Sulfide |
| Constituent Phase: | Sulfide, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
ND |
| Associated Effluent/ | ND |
| % Removal Efficiency (calculated): | Not Applicable |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Influent and effluent below the detection limit (1 mg/L) |
Notes: ND = non-detect
Data Set #56
Constituent Information
| Constituent: | Thallium |
| Constituent Phase: | Tl, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
6.93e-05 |
| Associated Effluent/ | ND |
| % Removal Efficiency (calculated): | 52.60 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Effluent below the detection limit (0.0000657 mg/L) |
Notes: ND = non-detect
Data Set #57
Constituent Information
| Constituent: | Thallium |
| Constituent Phase: | Tl, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
6.77e-05 |
| Associated Effluent/ | ND |
| % Removal Efficiency (calculated): | 51.48 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 0.0072 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Effluent below the detection limit (0.0000657 mg/L) |
Notes: ND = non-detect
Data Set #58
Constituent Information
| Constituent: | TOC |
| Constituent Phase: | Total Organic Carbon mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.638 |
| Associated Effluent/ | 7.2 |
| % Removal Efficiency (calculated): | -1028.53 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes: Influent estimated quantity
Data Set #59
Constituent Information
| Constituent: | Phosphorus |
| Constituent Phase: | P, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.368 |
| Associated Effluent/ | 1.88 |
| % Removal Efficiency (calculated): | -410.87 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #60
Constituent Information
| Constituent: | Total Suspended Solids |
| Constituent Phase: | TSS mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
10 |
| Associated Effluent/ | 8 |
| % Removal Efficiency (calculated): | 20.00 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #61
Constituent Information
| Constituent: | Uranium |
| Constituent Phase: | U, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.00666 |
| Associated Effluent/ | 0.00634 |
| % Removal Efficiency (calculated): | 4.80 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #62
Constituent Information
| Constituent: | Uranium |
| Constituent Phase: | U, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.0068 |
| Associated Effluent/ | 0.00627 |
| % Removal Efficiency (calculated): | 7.79 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 1.5 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #63
Constituent Information
| Constituent: | Vanadium |
| Constituent Phase: | V, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.00584 |
| Associated Effluent/ | 0.0057 |
| % Removal Efficiency (calculated): | 2.40 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #64
Constituent Information
| Constituent: | Zinc |
| Constituent Phase: | Zn, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.00686 |
| Associated Effluent/ | 0.00575 |
| % Removal Efficiency (calculated): | 16.18 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 0.12 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #65
Constituent Information
| Constituent: | Zinc |
| Constituent Phase: | Zn, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.00649 |
| Associated Effluent/ | 0.00652 |
| % Removal Efficiency (calculated): | -0.46 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
- Report
- FINAL, APPENDIX C, Phase 2 Treatability Study Report, Ultrafiltration/Reverse Osmosis and Biological Selenium Removal Fluidized Bed Bioreactor Treatment Technology
Source or source contact: Lynne Hood , Remedial Project Manager, Hood.Lynne@epa.gov, (208) 378-5757
Publication Date: February 2023
Document Type: PDF
Author: Formation Environmental
Prepared for: J.R. Simplot Company
Site Identifiers
| Site Name: | USDA FS CARIBOU-TARGHEE NF: SMOKY CANYON MINE SITE |
| EPA CERCLA ID: | IDN001002800 |
| Parent Name (if applicable): | SOUTHEAST IDAHO SELENIUM PROJECT/AKA SMOKY CANYON MINE (# IDN001002245) |
Miscellaneous Study Information
| Operable Unit (OU): | N/A |
| Sample Site ID: | LSSHS-ROC (influent) and LSSHS-BE2 (effluent from FBR #2) |
| Site Status: | Data not provided |
| Technology Tested: | Fluidized bed reactor (FBR) |
| Technology Type: | Active |
| Technology Name: | Fluidized bed reactor (FBR) |
| Pre-treatment or No Pre-treatment: | Pre-treatment |
| Source of MIW: | Groundwater springs (Hoopes Spring and South Fork Sage Creek spring) |
| Treatment Train? (Y/N): | Y |
| Specific Component for Performance Data: | FBR/part of treatment train with ultrafiltration (UF) and reverse osmosis (RO) pre-treatment |
| Technology Requirements: | Pumps to pump water from springs to treatment area. UF/RO (ultrafiltration/reverse osmosis) system to treat water prior to FBR |
| Geographic conditions/constraints: | Southeast Idaho. No constraints noted. |
| Scale: | Pilot |
| Duration of Study: | One sampling event (4/16/2016) |
Data Set #1
Constituent Information
| Constituent: | Boron |
| Constituent Phase: | B, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.04 |
| Associated Effluent/ | 0.0387 |
| % Removal Efficiency (calculated): | 3.25 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes: Estimated quantity
Data Set #2
Constituent Information
| Constituent: | COD |
| Constituent Phase: | Chemical Oxygen Demand mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
ND |
| Associated Effluent/ | 10 |
| % Removal Efficiency (calculated): | Not Applicable |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Influent below the detection limit (5 mg/L) |
Notes: ND = non-detect
Data Set #3
Constituent Information
| Constituent: | Total Dissolved Solids |
| Constituent Phase: | TDS mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
1150 |
| Associated Effluent/ | 1118 |
| % Removal Efficiency (calculated): | 2.78 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 1,134 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #4
Constituent Information
| Constituent: | Silver |
| Constituent Phase: | Ag, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
ND |
| Associated Effluent/ | ND |
| % Removal Efficiency (calculated): | Not Applicable |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 0.0034 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Influent and effluent below the detection limit (0.0000172 mg/L) |
Notes: ND = non-detect
Data Set #5
Constituent Information
| Constituent: | Silver |
| Constituent Phase: | Ag, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
ND |
| Associated Effluent/ | ND |
| % Removal Efficiency (calculated): | Not Applicable |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Influent and effluent below the detection limit (0.0000172 mg/L) |
Notes: ND = non-detect
Data Set #6
Constituent Information
| Constituent: | Aluminum |
| Constituent Phase: | Al, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
ND |
| Associated Effluent/ | ND |
| % Removal Efficiency (calculated): | Not Applicable |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Influent and effluent below the detection limit (0.0076 mg/L) |
Notes: ND = non-detect
Data Set #7
Constituent Information
| Constituent: | Aluminum |
| Constituent Phase: | Al, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.0098 |
| Associated Effluent/ | 0.0114 |
| % Removal Efficiency (calculated): | -16.33 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 0.39 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #8
Constituent Information
| Constituent: | Alkalinity |
| Constituent Phase: | Alkalinity as CaCO3 mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
780 |
| Associated Effluent/ | 790 |
| % Removal Efficiency (calculated): | -1.28 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #9
Constituent Information
| Constituent: | Ammonia |
| Constituent Phase: | Ammonia (as N) mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
ND |
| Associated Effluent/ | 3.52 |
| % Removal Efficiency (calculated): | Not Applicable |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Influent below the detection limit (0.026 mg/L) |
Notes: ND = non-detect
Data Set #10
Constituent Information
| Constituent: | Arsenic |
| Constituent Phase: | As, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.00142 |
| Associated Effluent/ | ND |
| % Removal Efficiency (calculated): | 85.99 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 0.01 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Effluent below the detection limit (0.000398 mg/L) |
Notes: ND = non-detect
Data Set #11
Constituent Information
| Constituent: | Arsenic |
| Constituent Phase: | As, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.00165 |
| Associated Effluent/ | 0.000629 |
| % Removal Efficiency (calculated): | 61.88 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 0.01 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #12
Constituent Information
| Constituent: | Boron |
| Constituent Phase: | B, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.0422 |
| Associated Effluent/ | 0.0424 |
| % Removal Efficiency (calculated): | -0.47 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 7 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes: Estimated quantity
Data Set #13
Constituent Information
| Constituent: | Barium |
| Constituent Phase: | Ba, Dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.203 |
| Associated Effluent/ | 0.202 |
| % Removal Efficiency (calculated): | 0.49 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #14
Constituent Information
| Constituent: | Barium |
| Constituent Phase: | Ba, Total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.211 |
| Associated Effluent/ | 0.21 |
| % Removal Efficiency (calculated): | 0.47 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 0.44 |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #15
Constituent Information
| Constituent: | Beryllium |
| Constituent Phase: | Be, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
ND |
| Associated Effluent/ | ND |
| % Removal Efficiency (calculated): | Not Applicable |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Influent and effluent below the detection limit (0.000047 mg/L) |
Notes: ND = non-detect
Data Set #16
Constituent Information
| Constituent: | Beryllium |
| Constituent Phase: | Be, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
ND |
| Associated Effluent/ | ND |
| % Removal Efficiency (calculated): | Not Applicable |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 0.0067 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Influent and effluent below the detection limit (0.000047 mg/L) |
Notes: ND = non-detect
Data Set #17
Constituent Information
| Constituent: | BOD |
| Constituent Phase: | Biochemical Oxygen Demand mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
ND |
| Associated Effluent/ | 27 |
| % Removal Efficiency (calculated): | Not Applicable |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Influent below the detection limit (2 mg/L) |
Notes: ND = non-detect
Data Set #18
Constituent Information
| Constituent: | Calcium |
| Constituent Phase: | Ca, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
244 |
| Associated Effluent/ | 242 |
| % Removal Efficiency (calculated): | 0.82 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #19
Constituent Information
| Constituent: | Cadmium |
| Constituent Phase: | Cd, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
ND |
| Associated Effluent/ | ND |
| % Removal Efficiency (calculated): | Not Applicable |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 0.005 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Influent and effluent below the detection limit (0.0000362 mg/L) |
Notes: ND = non-detect
Data Set #20
Constituent Information
| Constituent: | Cadmium |
| Constituent Phase: | Cd, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
6.54e-05 |
| Associated Effluent/ | ND |
| % Removal Efficiency (calculated): | 72.32 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 0.005 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Effluent below the detection limit (0.0000362 mg/L) |
Notes: ND = non-detect, estimated quantity
Data Set #21
Constituent Information
| Constituent: | Chloride |
| Constituent Phase: | Cl mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
38.3 |
| Associated Effluent/ | 38.1 |
| % Removal Efficiency (calculated): | 0.52 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #22
Constituent Information
| Constituent: | Cobalt |
| Constituent Phase: | Co, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.000319 |
| Associated Effluent/ | 0.0084 |
| % Removal Efficiency (calculated): | -2533.23 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #23
Constituent Information
| Constituent: | Cobalt |
| Constituent Phase: | Co, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.000315 |
| Associated Effluent/ | 0.00771 |
| % Removal Efficiency (calculated): | -2347.62 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 0.1 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #24
Constituent Information
| Constituent: | Chromium |
| Constituent Phase: | Cr, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.00236 |
| Associated Effluent/ | 0.00165 |
| % Removal Efficiency (calculated): | 30.08 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 0.074 mg/L (Cr III); 0.011 mg/L (Cr VI) |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #25
Constituent Information
| Constituent: | Chromium |
| Constituent Phase: | Cr, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.0029 |
| Associated Effluent/ | 0.00196 |
| % Removal Efficiency (calculated): | 32.41 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #26
Constituent Information
| Constituent: | Copper |
| Constituent Phase: | Cu, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.000188 |
| Associated Effluent/ | 0.000494 |
| % Removal Efficiency (calculated): | -162.77 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 0.011 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes: Estimated quantity
Data Set #27
Constituent Information
| Constituent: | Copper |
| Constituent Phase: | Cu, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.000925 |
| Associated Effluent/ | 0.00132 |
| % Removal Efficiency (calculated): | -42.70 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #28
Constituent Information
| Constituent: | Fluoride |
| Constituent Phase: | F mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.464 |
| Associated Effluent/ | 1.59 |
| % Removal Efficiency (calculated): | -242.67 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #29
Constituent Information
| Constituent: | Iron |
| Constituent Phase: | Fe, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
ND |
| Associated Effluent/ | ND |
| % Removal Efficiency (calculated): | Not Applicable |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Influent and effluent below the detection limit (0.01 mg/L) |
Notes: ND = non-detect
Data Set #30
Constituent Information
| Constituent: | Iron |
| Constituent Phase: | Fe, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.0875 |
| Associated Effluent/ | 0.0309 |
| % Removal Efficiency (calculated): | 64.69 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 1 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #31
Constituent Information
| Constituent: | Hardness |
| Constituent Phase: | Hardness mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
983 |
| Associated Effluent/ | 980 |
| % Removal Efficiency (calculated): | 0.31 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #32
Constituent Information
| Constituent: | Mercury |
| Constituent Phase: | Hg, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
6.3e-05 |
| Associated Effluent/ | 5.6e-05 |
| % Removal Efficiency (calculated): | 11.11 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 0.00077 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #33
Constituent Information
| Constituent: | Mercury |
| Constituent Phase: | Hg, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
5.2e-05 |
| Associated Effluent/ | 5.6e-05 |
| % Removal Efficiency (calculated): | -7.69 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #34
Constituent Information
| Constituent: | Potassium |
| Constituent Phase: | K, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
3.44 |
| Associated Effluent/ | 3.33 |
| % Removal Efficiency (calculated): | 3.20 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #35
Constituent Information
| Constituent: | Magnesium |
| Constituent Phase: | Mg, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
92.9 |
| Associated Effluent/ | 92.2 |
| % Removal Efficiency (calculated): | 0.75 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #36
Constituent Information
| Constituent: | Manganese |
| Constituent Phase: | Mn, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.00166 |
| Associated Effluent/ | 0.00641 |
| % Removal Efficiency (calculated): | -286.14 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 1.65 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #37
Constituent Information
| Constituent: | Manganese |
| Constituent Phase: | Mn, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.00187 |
| Associated Effluent/ | 0.00621 |
| % Removal Efficiency (calculated): | -232.09 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #38
Constituent Information
| Constituent: | Molybdenum |
| Constituent Phase: | Mo, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.0043 |
| Associated Effluent/ | 0.00523 |
| % Removal Efficiency (calculated): | -21.63 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #39
Constituent Information
| Constituent: | Molybdenum |
| Constituent Phase: | Mo, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.00395 |
| Associated Effluent/ | 0.00562 |
| % Removal Efficiency (calculated): | -42.28 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 3.2 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #40
Constituent Information
| Constituent: | Sodium |
| Constituent Phase: | Na, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
29.4 |
| Associated Effluent/ | 28.3 |
| % Removal Efficiency (calculated): | 3.74 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #41
Constituent Information
| Constituent: | Nickel |
| Constituent Phase: | Ni, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.00108 |
| Associated Effluent/ | 0.00849 |
| % Removal Efficiency (calculated): | -686.11 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 0.052 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #42
Constituent Information
| Constituent: | Nickel |
| Constituent Phase: | Ni, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
ND |
| Associated Effluent/ | 0.0073 |
| % Removal Efficiency (calculated): | Not Applicable |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Influent below the detection limit (0.0000533 mg/L) |
Notes: ND = non-detect
Data Set #43
Constituent Information
| Constituent: | Nitrate |
| Constituent Phase: | as N (NO3) mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
1.23 |
| Associated Effluent/ | 0.24 |
| % Removal Efficiency (calculated): | 80.49 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #44
Constituent Information
| Constituent: | Nitrate + Nitrite |
| Constituent Phase: | NO3 + NO2 mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
1.23 |
| Associated Effluent/ | 0.238 |
| % Removal Efficiency (calculated): | 80.65 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #45
Constituent Information
| Constituent: | Lead |
| Constituent Phase: | Pb, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
ND |
| Associated Effluent/ | ND |
| % Removal Efficiency (calculated): | Not Applicable |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 0.0025 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Influent and effluent below the detection limit (0.0000554 mg/L) |
Notes: ND = non-detect
Data Set #46
Constituent Information
| Constituent: | Lead |
| Constituent Phase: | Pb, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
ND |
| Associated Effluent/ | ND |
| % Removal Efficiency (calculated): | Not Applicable |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Influent and effluent below the detection limit (0.0000554 mg/L) |
Notes: ND = non-detect
Data Set #47
Constituent Information
| Constituent: | Antimony |
| Constituent Phase: | Sb, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
8.09e-05 |
| Associated Effluent/ | 7.32e-05 |
| % Removal Efficiency (calculated): | 9.52 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #48
Constituent Information
| Constituent: | Antimony |
| Constituent Phase: | Sb, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
7.34e-05 |
| Associated Effluent/ | 7.32e-05 |
| % Removal Efficiency (calculated): | 0.27 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 0.24 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #49
Constituent Information
| Constituent: | Selenium |
| Constituent Phase: | Selenium, +6 (Selenate) mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.599 |
| Associated Effluent/ | 7e-05 |
| % Removal Efficiency (calculated): | 99.99 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes: Effluent is estimated quantity
Data Set #50
Constituent Information
| Constituent: | Selenium |
| Constituent Phase: | Selenium, +4 (Selenite) mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
ND |
| Associated Effluent/ | 0.000967 |
| % Removal Efficiency (calculated): | Not Applicable |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Influent below the detection limit (0.00005 mg/L) |
Notes: ND = non-detect
Data Set #51
Constituent Information
| Constituent: | Selenium |
| Constituent Phase: | Se, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.62 |
| Associated Effluent/ | 0.00722 |
| % Removal Efficiency (calculated): | 98.84 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #52
Constituent Information
| Constituent: | Selenium |
| Constituent Phase: | Se, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.574 |
| Associated Effluent/ | 0.0109 |
| % Removal Efficiency (calculated): | 98.10 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | 98% |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y, for this data point; N for overall system performance over a longer period did not meet with average effluent of 0.024 mg/l |
| Performance Metrics: | 0.0167 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #53
Constituent Information
| Constituent: | Sulfate |
| Constituent Phase: | Sulfate (SO42-) mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
219 |
| Associated Effluent/ | 226 |
| % Removal Efficiency (calculated): | -3.20 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #54
Constituent Information
| Constituent: | Sulfide |
| Constituent Phase: | Sulfide, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
ND |
| Associated Effluent/ | ND |
| % Removal Efficiency (calculated): | Not Applicable |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Influent and effluent below the detection limit (1 mg/L) |
Notes: ND = non-detect
Data Set #55
Constituent Information
| Constituent: | Thallium |
| Constituent Phase: | Tl, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
6.93e-05 |
| Associated Effluent/ | ND |
| % Removal Efficiency (calculated): | 52.60 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Effluent below the detection limit (0.0000657 mg/L) |
Notes: ND = non-detect
Data Set #56
Constituent Information
| Constituent: | Thallium |
| Constituent Phase: | Tl, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
6.77e-05 |
| Associated Effluent/ | ND |
| % Removal Efficiency (calculated): | 51.48 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 0.0072 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Effluent below the detection limit (0.0000657 mg/L) |
Notes: ND = non-detect
Data Set #57
Constituent Information
| Constituent: | TOC |
| Constituent Phase: | Total Organic Carbon mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.638 |
| Associated Effluent/ | 7.65 |
| % Removal Efficiency (calculated): | -1099.06 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes: Influent estimated quantity
Data Set #58
Constituent Information
| Constituent: | Phosphorus |
| Constituent Phase: | P, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.368 |
| Associated Effluent/ | 1.94 |
| % Removal Efficiency (calculated): | -427.17 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #59
Constituent Information
| Constituent: | Total Suspended Solids |
| Constituent Phase: | TSS mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
10 |
| Associated Effluent/ | 10 |
| % Removal Efficiency (calculated): | 0.00 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #60
Constituent Information
| Constituent: | Uranium |
| Constituent Phase: | U, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.00666 |
| Associated Effluent/ | 0.00639 |
| % Removal Efficiency (calculated): | 4.05 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #61
Constituent Information
| Constituent: | Uranium |
| Constituent Phase: | U, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.0068 |
| Associated Effluent/ | 0.00671 |
| % Removal Efficiency (calculated): | 1.32 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 1.5 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #62
Constituent Information
| Constituent: | Vanadium |
| Constituent Phase: | V, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.00584 |
| Associated Effluent/ | 0.00548 |
| % Removal Efficiency (calculated): | 6.16 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #63
Constituent Information
| Constituent: | Vanadium |
| Constituent Phase: | V, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.00762 |
| Associated Effluent/ | 0.00732 |
| % Removal Efficiency (calculated): | 3.94 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 0.027 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #64
Constituent Information
| Constituent: | Zinc |
| Constituent Phase: | Zn, dissolved mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.00686 |
| Associated Effluent/ | 0.00733 |
| % Removal Efficiency (calculated): | -6.85 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Y |
| Performance Metrics: | 0.12 mg/L |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
Data Set #65
Constituent Information
| Constituent: | Zinc |
| Constituent Phase: | Zn, total mg/L |
| Reported as Load (Y/N): | N |
Pond Depth: N/A
Max influent/associated effluent
| Max. Influent/ |
0.00649 |
| Associated Effluent/ | 0.00811 |
| % Removal Efficiency (calculated): | -24.96 |
Min influent/associated effluent
| Min. Influent/ |
Data not provided |
| Associated Effluent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Max effluent/associated influent
| Max. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated) | Not Applicable |
Min effluent/associated influent
| Min. Effluent/ |
Data not provided |
| Associated Influent/ | Data not provided |
| % Removal Efficiency (calculated): | Not Applicable |
Avg. influent concentration/associated time
| Avg. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Med. influent concentration/associated time
| Med. Influent/ |
Data not provided |
| Avg. Associated Time (Influent/ |
Data not provided |
Avg. effluent concentration/associated time period
| Avg. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Med. effluent concentration/associated time period
| Med. Effluent/ |
Data not provided |
| Avg. Associated Time (Effluent/ |
Data not provided |
Parameters and water chemistry associated with documented concentrations
| Avg Percent Removal (reported): | Data not provided |
| Influent/Pre/Upgradient or Effluent/ | Data not provided |
| pH: | Data not provided |
| DO: | Data not provided |
| Water Temperature: | Data not provided |
| Air Temperature: | Data not provided |
| Eh: | Data not provided |
| ORP: | Data not provided |
| Specific Conductivity: | Data not provided |
| Other Parameters: | None N/A |
Load Information
| Loads Treated: | Data not provided |
| Flows treated: | Data not provided |
| Flow rate: | Data not provided |
Treatment Evaluation
| Were treatment goals met? (Y/N): | Data not provided |
| Performance Metrics: | Data not provided |
| Limitations/Constraints: | Data not provided |
| Longevity Estimates: | Data not provided |
| Lessons Learned: | Data not provided |
| Reported Cost Data: | Construct 2,000 gpm UF/RO FBR Treatment System ($22M); total capital costs for entire system $29.7M, Annual O&M for entire system $1.56M |
| Other design details: | During operation, a carbon source, micronutrients, ammonium sulfate, and phosphoric acid were added to the RO concentrate water prior to being delivered to the FBRs. The dosage and nutrient feed rates were adjusted to maintain ORP in the range of -200 to -500 millivolts (mV), pH in the range of 6 to 9, and DO near 0 mg/L (the bioreactors are anaerobic) within the FBRs for optimum selenium reduction. |
| Other performance details: | Overall system is anticipated with ongoing maintenance and optimization to maintain removal of 90-95%. Specifics for FBR are not provided |
| Limitations to data found: | Data not provided |
Notes:
| °C | degrees Celsius |
| °F | degrees Fahrenheit |
| µg/L | micrograms per liter |
| µmhos/cm | micromhos per centimeter |
| µS/cm | microSiemens per centimeter |
| Ag | Silver |
| Al | Aluminum |
| As | Arsenic |
| AWQC | Ambient Water Quality Criteria |
| B | Boron |
| Ba | Barium |
| BCR | Biochemical Reactor |
| Be | Beryllium |
| BOD | Biochemical Oxygen Demand |
| CaCO3 | Calcium carbonate |
| CERCLA | Comprehensive Environmental Response, Compensation, and Liability Act |
| cfs | cubic feet per second |
| CHIT | Chitorem® |
| Cl | Chloride |
| Co | Cobalt |
| CO3 | Carbon trioxide |
| COC | Constituent of Concern |
| COD | Chemical Oxygen Demand |
| Cr | Chromium |
| Cu | Copper |
| DOC | Dissolved Organic Carbon |
| EPA | Environmental Protection Agency |
| F | Fluoride |
| FBR | Fluidized Bed Reactor |
| Fe | Iron |
| ft | feet |
| gpm | gallons per minute |
| GW | Groundwater |
| HCO3 | Bicarbonate |
| Hg | Mercury |
| K | Potassium |
| lbs | pounds |
| Mg | Magnesium |
| MG | Million Gallons |
| Mg(OH)2 | Magnesium hydroxide |
| mg/L | milligrams per liter |
| Mn | Manganese |
| Mo | Molybdenum |
| mV | millivolts |
| N | Nitrogen |
| N/A | not applicable |
| Na | Sodium |
| NA | Not available |
| ND | Not detected |
| Ni | Nickel |
| NO3 | Nitrate |
| NO3 + NO2 | Nitrate + Nitrite |
| NR | Not reported |
| NTU | Nephelometric Turbidity Unit |
| OH | Hydroxide |
| OU | Operable Unit |
| P | Phosphorus |
| Pb | Lead |
| PRB | Permeable Reactive Barrier |
| RA | Remedial Action |
| RO | Reverse osmosis |
| SAPS | Successive Alkalinity Producing System |
| Sb | Antimony |
| Se | Selenium |
| SO42- | Sulfate |
| SRB | Sulfate Reducing Bacteria |
| STC | Seep Treatment Cell |
| TDS | Total Dissolved Solids |
| TOC | Total Organic Carbon |
| TSS | Total Suspended Solids |
| U | Uranium |
| UF | Ultra-filtration |
| V | Vanadium |
| VFR | Vertical Flow Reactor |
| Zn | Zinc |
| Label | Description |
|---|---|
| Site Name | Name of the site |
| EPA CERCLA ID | EPA CERCLA ID number |
| Parent Name | If the test was conducted at a 'child' site or an alias, this is the name of the larger associated Superfund site. |
| Operable Unit (OU) | Specific operable unit (OU) of the site if specified |
| Technology Tested | Name of the technology tested |
| Technology Type | The technology type (i.e., active or passive/semi-passive) |
| Source of MIW | Source of the MIW (e.g., adit drainage, groundwater) |
| Treatment Train? (Y/N) | Whether the treatment was a treatment train (i.e., multiple individual technologies) |
| Specific Component for Performance Data | Component for which data are reported |
| Technology Requirements | Requirements of the technology (e.g., electricity, pH > or < X, dissolved oxygen < X, etc.) |
| Geographic conditions/ constraints | Geographic conditions/constraints (e.g., topography, climate) |
| Scale | Scale of the technology (e.g., pilot, or full-scale application) |
| Duration of Study | Length of the study |
| Constituent | Element or ion treated |
| Constituent Phase | Identity - contaminants of concern (COCs) and others having data/information on treatment |
| Unit | Unit of concentration reported in study |
| Max. Influent Concentration | Maximum influent concentration treated |
| Associated Effluent Concentration | Effluent concentration attained for maximum concentration treated |
| Max. Effluent Concentration | Maximum effluent concentration treated |
| Associated Influent Concentration | Influent concentration attained for maximum concentration treated |
| Min. Influent Concentration | Minimum influent concentration treated and |
| Associated Effluent Concentration | Effluent concentration attained for maximum concentration treated |
| Min. Effluent Concentration | Minimum effluent concentration treated and |
| Associated Influent Concentration | Influent concentration attained for maximum concentration treated |
| Avg. Influent Concentration | Average influent concentration treated and associated time |
| Avg. Associated Time (Influent) | Time over which average X was calculated |
| Med. Influent Concentration | Median influent concentration treated and associated time |
| Avg. Associated Time Influent) | Time over which average X was calculated |
| Avg. Effluent Concentration | Average effluent concentration treated and associated time |
| Avg. Associated Time (Effluent) | Time over which average X was calculated |
| Med. Effluent Concentration | Median effluent concentration treated and associated time |
| Avg. Associated Time (Effluent) | Time over which average X was calculated |
| Avg. Percent Removal | Average percent removal |
| Parameters | Parameters associated with the concentrations of other data documented |
| Loads Treated | Mass of constituent per unit flow |
| pH | pH associated with documented concentrations |
| DO | DO associated with documented concentrations |
| Water Temperature | Water temperature associated with documented concentrations |
| Air Temperature | Air temperature associated with documented concentrations |
| ORP | Oxidation-reduction potential associated with documented concentrations |
| Specific Conductivity | Specific conductivity associated with documented concentrations |
| Flows treated | Flows treated |
| Were treatment goals met? (Y/N) | Whether the testing met the treatment goals |
| Performance Metrics | Goals or performance metrics upon which the treatment success was based |
| Limitations/Constraints | Any limitations or constraints noted that contributed to success or failure |
| Longevity Estimates | Estimates of longevity, if provided |
| Lessons Learned | Any reported lessons learned |
| Reported Cost Data | Any reported cost data |
| Other design details | Any other design details provided in the sources cited |
| Other performance details | Any other performance details provided in the sources cited |
| Limitations to the found data | Limitations to the data found (e.g., data in the source only presented as averages, so was unable to report maximum influent treated with corresponding effluent attained) |
| Notes | Any notes |