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Effective Use Of Peracetic Acid to Reduce Effluent Disinfection Byproduct in Water Resource Recovery Facilities Isaiah Shapiro, EIT Dimitri Katehis PhD, PE Dave Hagan, PE
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Outline Background and Problem Identification Evaluation Approach Bench and Pilot Scale Testing Conclusion
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Outline Background and Problem Identification Evaluation Approach Bench and Pilot Scale Testing Conclusion
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City of Largo Located in Pinellas County 4 th largest City in Tampa Bay Serves about 75,000 residents
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WASTEWATER RECLAMATION FACILITY Advance Wastewater Treatment Plant (AWTP) –BOD:TSS:TN:TP = 5:5:3:1 Influent Flow –Permitted: 18 MGD –Current: 12.5 MGD Effluent Discharge –Reuse: 50% –Surface Water Discharge: 50% Headworks Primary Clarifiers A2O Process Secondary Clarifiers ABW Filters Deep Bed Filters Disinfection & Dechlorination Reuse or SWD
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Expanded Environmental Stewardship Goals Florida Department of Environmental Protection (FDEP) More stringent regulation of disinfection byproducts (DBPs) in the surface water discharge –bromo-dichloro-methane (BDCM) Existing Disinfection System –Chlorination with gaseous chlorine –Dechlorination with sulfur dioxide
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Effluent BCDM Limits
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Outline Background and Problem Identification Evaluation Approach Bench and Pilot Scale Testing Conclusion
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Evaluation Objective Reduce the effluent BDCM discharged to surface waters –Annual Average BCDM Limit Interim: 30 μg/L Final: 22 μg/L Provide an efficient and effective means of disinfection
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Why not just UV? High Concentration of Dissolved Organics Very low UVT (38%) Low UVT mostly on wet weather flows Typical design UVT: 55- 65% Double the cost ($$$)
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Evaluation Approach Alternative Approaches: –Reduce Precursor (i.e. Dissolved Organics) –Replace Gaseous Chlorine –Remove BCDM after it forms Treatment Configurations: –Full Flow Treatment –Split Flow Treatment
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Split Flow Treatment
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Many Options ChlorineFull Flow Remove Precursor OzoneGAC/PACMIEX Replace Chlorine OzonePAAImprove UVTOzone/UVPAA/UVGAC/PAC/UVFerrate/UVMIEX//UVRemove DBPsGAC/PACAerationOther Split Flow Same 31 Alternatives Evaluated
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Outline Background and Problem Identification Evaluation Approach Bench and Pilot Scale Testing Conclusion
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Preliminary Evaluation Technology Disinfection Precursor Removal BDCM Removal Bench Scale Testing Ozone Hydrogen Peroxide MIEX PAC/GAC Ferrate PAA Desktop Studies Coagulation Aeration
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Viable Alternatives ConfigurationAlternatives Full Flow Treatment (FT)Ozone Split Flow Treatment (ST) Ozone + NaOCl PAA + NaOCl UV (48% UVT) + NaOCl
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Non-Cost Criteria Analysis
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Viable Alternatives - Costs 5% Interest, 20 Years ConfigurationAlternativesPW - 20% Present Worth PW + 35% Full Flow Treatment (FT) Ozone$14.9M$16.7M$19.8M Split Flow Treatment (ST) Ozone + NaOCl$12.7M$14.2M$16.8M PAA + NaOCl$11.7M$12.2M$13.1M UV (48% UVT) + NaOCl $14.7M$16.1M$18.5M
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Pilot Testing – UV and Ozone BCDM Reduction –Ozone was not able to reduce BCDM below 22 μg/L Dose up to 7 mg/L Precursor Removal: –Increase the filter effluent UVT from 45% to 55% Dose up to 10 mg/L Advanced Oxidation Unit
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Pilot Testing – UV and Ozone UVT Response to Applied Ozone Dose
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PAA Pilot Testing 18,000-gallon Baffled Contact Tank Solvay Proxitane® WW-12 PAA ComponentConcentration (% by wt) Peracetic Acid12 Hydrogen Peroxide18.5 Acetic Acid15
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PAA Pilot Testing Theoretical Detention Times –15 min, 30 min & 45 min Dye Testing –Hydraulic Short Circuiting Actual Detention Times –2 min, 4 min & 7 min Dosage Range: –1.0 to 4.0 mg/L
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PAA Pilot Testing Date PAA Dose, mg/L DT, min.Inf./Eff. BDCM μg/L TTHM μg/L T HAA μg/L Bromate μg/L 26-Jul3.54Influent4.1204.65.0U 26-Jul3.54Effluent3.9197.35.0U 27-Jul3.07Influent4.8203.95.0U 27-Jul3.07Effluent4.2186.85.0U Results
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Follow Up Bench Scale Testing Refining dose: 2.5 mg/L to 3.5 mg/L Actual contact time of 15 min to 30 min Blend Samples BDCM & Residual PAA or Cl2 Sample Add Hypo Dose Wait 15 min BDCM & Residual Chlorine Sample Add PAA Dose Wait 15 min BDCM & Residual PAA
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What happens when NaOCl and PAA mix? Solution No.SampleDose (mg/L) 15-min. Residual (mg/L) BDCM (µg/L) -Filtered effluent001.9 1Filtered effluent2.5 PAA1.0 PAA1.6 2Filtered effluent3.5 PAA1.3 PAA1.6 3Filtered effluent12 -Cl22.2 Cl214 4Filtered effluent9 - Cl21.3 Cl215 1 & 3BlendNA0.027.7 1 & 4BlendNA0.016.7 2 & 3BlendNA0.017.1 2 & 4BlendNA0.026.8
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Results of Pilot Testing Peracetic Acid (PAA) –Effective dosages 3.0 mg/l @ 30 min 3.5 mg/L @ 15 min –Effective reduction of DBPs –No increase of toxicity (WET Testing) –Minor to no impact on BOD, Turbidity, Conductivity or pH –Increases the DO of the effluent (1 to 5 mg/L) –Little need for quenching of PAA residual when mixed with chlorine residual
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Outline Background and Problem Identification Evaluation Approach Bench and Pilot Scale Testing Conclusion
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PAA can be a cost-effective high level disinfection alternative to reduce disinfection by-products Split treatment option provides: –Reliability –Flexibility –Cost Control
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Where are we today? Operations Permit Modification (2014) Final Design (2014) Award May 2015 ($13.7 M)
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Acknowledgements Freddy Betancourt, PE, LEED AP, ENV SP – Greeley and Hansen David Hagan, PE – Greeley and Hansen Leland Dicus, PE – City of Largo Chuck Mura, PE – City of Largo Our partners at CDM Smith Special Thanks! Bob Freeborn, Peragreen Solutions John Maziuk, Solvay Chemicals
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Thank You!
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