Potential of Advanced Oxidation Processes (AOP) for Simultaneous Disinfection and Polishing of Drinking Water

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Potential of Advanced Oxidation Processes (AOP) for Simultaneous Disinfection and Polishing of Drinking Water ASCE New Orleans Branch LA Civil Engineering Conference & Show, Kenner, LA September 13, 2002 Jennifer E. Holland Tulane University, New Orleans, LA Glen R. Boyd, Ph.D., PE Dept. of Civil & Environmental Engineering Robert S. Reimers, Ph.D. FAIC Andrew J. Englande,, Ph.D., P.E. Dept. of Environmental Health Sciences

Introduction Scope of Presentation Potential application of advanced oxidation processes (AOP) for drinking water treatment Specific Objectives 1. Overview of conventional treatment for disinfection and micropollutants 2. EDCs/PPCPs as emerging micropollutants 3. Potential applications of AOP in meeting conventional treatment goals for micropollutants 4. Ongoing research at Tulane University

Outline Background Micropollutants - EDC/PPCPs Conventional WT Ongoing Research at Tulane Methods Occurrence of EDC/PPCP in SE Louisiana Advanced Oxidation Processes (AOPs( AOPs) Preliminary Conclusions Next Steps

Background - Contaminated Micropollutants Drinking Water Sources Pesticides, fertilizers, industrial solvents Toxics, carcinogens Typical concentrations in Miss River Water Atrazine = 1 ppb (Source: Goolsby and Pereira, USGS) Seasonal characteristics (e.g., storm events) Atrazine = 7 ppb MCL = 3 ppb (Source: Goolsby and Pereira, USGS) Emerging low-level level contaminants Endocrine disrupting chemicals (EDCs( EDCs) Pharmaceuticals and personal care products (PPCPs) Barber et al., www.usgs.gov

Background-- --EDCs Chemicals which affect the endocrine system Trussel, R. R. 2001, JAWWA 93(2):58-65

Background - Micropollutants Why are low levels of EDCs a cause for concern? DOSE RESPONSE Dose Calculation Theoretical Concentration in Drinking Water Source = 100 ppt (ng/l) 70 kg Adult drinks 2 L of water per day Vom Saal et al., 1997 http://www.safewater.org/conferences/proceeding s/lawrence.htm Dose = (100 * 2)/70,000 = 0.003 ng/g

Background-- --Micropollutants Synergistic effect of mixture of EDCs? --> > 0.003 ng/g dose?

Background Conventional WT Some PPCPs/EDCs are soluble and refractory--> not removed by conventional water treatment J. Lawrence Drinking Water Treatment Present and Future Developments http://www.safewater.org/conferences/proceedings/lawrence.htm

Background Chlorine in Conventional WT Chlorine does kill harmful microorganisms Fecal coliform E. coli Entercocci Does not kill protozoan oocysts Cryptosporidium Giardia

Background-- --Chlorine for Conventional WT Chlorine combines with natural organic matter (NOM) to form disinfection byproducts (DBPs( DBPs) Trihalomethanes (THMs) Effects of Cl 2 on organic micropollutants (EDC/PPCPs)? Possible formation of chlorinated metabolites Need more research

Background Conventional WT Granular Activated Carbon (GAC) May be used to remove organics Adsorbs organic chemicals Dependent on solubility of chemical Many drugs designed to be highly water soluble (check K ow ) Can be used at water treatment plant Highly expensive Must be regenerated Also implemented at point of use (Brita, Pur)

Background - AOPs Advanced Oxidation Processes -- generate free radicals (OH, O 3, OH 2 ) Hydroxyl radicals indiscriminately oxidize organic matter Recalcitrant organics Cell walls of protozoan oocysts Process combines disinfection/oxidation into one step May be more effective than Cl 2 and GAC

Background - AOPs Oxidant Hydroxyl Radical (OH ) Ozone (O 3 ) Hydrogen Peroxide (H 2 O 2 ) Chlorate (ClO 4 ) Chlorite (ClO 3 ) Chlorine Dioxide (ClO 2 ) Chlorine (Cl 2 /OCl - ) Oxidizing Power (V) 2.6 2.1 1.8 1.7 1.7 1.7 1.6

Research at Tulane EDC/PPCPs in Source Waters Target Compounds and Detection Limits Target compounds and Method Detection Limits (MDL) Target Compound IDL [ng/l] Average % Recov. % RSD Compl of Deriv (%) MDL* [ng/l] Clofibric acid 3 60.8 12.6 100 0.6 Estrone 3 91.9 5.1 100 0.5 17β-Estradiol 1 90.5 9.1 100 0.1 Ibuprofen 13 47.1 26.9 0 3.5 Naproxen 3 87.9 2.8 0 0.4 Acetaminophen 45 N.D. N.D. 100 N.D. Bisphenol-A 0.6 99.7 3.5 100 0.1 Chlorophene 0.6 71.7 5.9 100 0.1 Triclosan 1 53.8 24 100 0.2

Research at Tulane EDC/PPCPs Monitoring Lake Pontchartrain & Mississippi River Sampling Site Lake Pontchartrain Mississippi River date 9/14/01 9/24/01 9/14/01 9/24/01 Target Compound ng/l ng/l ng/l ng/l Naproxen 107 22 37 39 Bisphenol-A-d14* 13.6% 13.9% 68.0% 75.0% Estrone-d4* 52.6% 28.9% 103.4% 119.4% Acetaminophen-d4* 1.1% 1.2% N.D. N.D.

Research at Tulane AOPs Bench Scale Experiments Comparison of four different AOPs: 1. Peroxone O 3 + H 2 O 2 OH 2. Ozone plus UV O 3 + UV OH 3. Hydrogen Peroxide plus UV H 2 O 2 + UV OH 4. Mixed Oxidants High energy vapor including OH

Research at Tulane - AOPs oxygen feed gas (P, Q) ozone generator (P, Q) ozone monitor stabilization tank (T, P) Mixed oxidant generator chiller (T) 3-way valve 254 nm UV lamp ozone destruction chamber ozone monitor contact chamber diffuser water recirculation sampling valve

Research at Tulane - AOPs Preliminary Conclusions Mixed oxidants have a slightly greater oxidizing power than ozone alone Mixed oxidants are an effective disinfectant Mixed oxidants were more effective in the oxidation of micropollutants (MTBE) than ozone alone-- more research needed

Methods Use AOPs bench scale apparatus to investigate removal of EDC and PPCP micropollutants Naproxyn 17β-Estradiol Bisphenol-A Spike DI water samples 0 to 10 µg/l Spike Mississippi River samples 10 to 100 ng/l Isolate using SPE, derivatize using BSTFA, analyze using GC/MS

Methods - Naproxyn Anti-inflammatory inflammatory prescription drug No known endocrine disrupting effects Log K ow ~ 3.10

Methods - 17β-Estradiol Hormone Endocrine Disruptor Log K ow = 3.94

Methods - Bisphenol-A Plasticizing agent Suspected endocrine disruptor Log K ow = 3.32

Methods Overview of Experiments Study each compound separately in a DI water matrix Determine doses of ozone, peroxide, UV light and mixed oxidants required for complete mineralization Compare material and power costs of AOPs to Cl 2 and GAC estimated values

Preliminary Conclusions AOPs may be a more cost effective means to disinfect and polish potable water compared to chlorine and GAC Data from bench scale experiments at Tulane University may be used in the design of a pilot scale AOP system for New Orleans drinking water

Next Steps Oct 2002 Dec 2002 Mar 2003 June 2003 Complete ongoing AOP experiments-- optimization of Tulane mixed oxidant process Develop laboratory standards and analytical procedures for EDC/PPCP micrpollutants Complete AOP experiments for treatment of spiked DI and Miss. R. water samples Compare results to GAC data

Acknowledgements Severn Trent Services, Inc. Gordon Austin, Peter Brown, Glenn Semel - New Orleans Sewerage and Water Board Dr. D. Grimm - Coordinated Instrumentation Facility, Tulane University Helge Reemstma, Bingen University, Germany