Trihalomethanes Removal Evaluation

Slides:



Advertisements
Similar presentations
Amherst , MA, Drinking Water System Atkins Water Treatment Plant
Advertisements

Often water is prescreened, treated with ozone, or pre-chlorinated before entering the coagulation basin (depending on the quality of the water). Coagulation.
Disinfectant & Disinfection Byproducts Control and Optimization Case Study of the University of Alaska Fairbanks Water System By Johnny Mendez, P.E., Drinking.
LEACHATE MANAGEMENT AND TREATMENT
Reducing THM via Aeration: A Case Study November 21, 2013 by Gary Williams, P.E. Jones & Henry Engineers Southeast AWWA District Meeting 1.
Case Study: Disinfection byproducts in a recently constructed public water supply Maria O’Connell, P.E. Kristine Wheeler, P.E. New York State Department.
Disinfection by-products Precursors + oxidant → DBPs DBPs can be reduced by: the precursors (organic materials present in the sourcewater) the reactants.
Calcite Contactors for Corrosion Control
HOW DISINFECTION WORKS. Disinfection kills or inactivates living organisms that cause disease Oxidation destroys the physical structure of the organism.
CO ‑ STAR: Colorado Strategy for Arsenic Reduction A Five Phase Compliance Assistance Program 1. Evaluate 2. Sample 3.Engineer4. Finance 5. Implement.
Slide 1 Delta Water Quality: Implications for Utility Compliance with the Safe Drinking Water Act Edward G. Means III Sr. Vice President McGuire Environmental.
Water Distribution Systems Water Quality Modelling for Civil Engineers 1 Helena M Jetmarova, GWMWater Helena M Jetmarova, GWMWater George J Kastl, MWH.
Water Treatment for NYC Croton Schematic. NYC Filtration Plant for Delaware and Catskill Systems  Filtration avoidance criteria  Alternatives to Filtration.
Math for Water Technology MTH 082 (pg. 468)
Water Treatment for NYC Croton Schematic. NYC Filtration Plant for Delaware and Catskill Systems ä Filtration avoidance criteria ä Alternatives to Filtration.
NYC Filtration Plant for Delaware and Catskill Systems ä Filtration avoidance criteria ä Alternatives to Filtration? ä Where should the plant(s) be located?
Drinking Water and the Lake There are 40+ plants utilizing Lake Michigan Water Illinois, Wisconsin, Michigan, Indiana Sizes of 1 MGD to 1 BGD Designed.
Combined Ozonation-Nanofiltration for Drinking Water Treatment B. S
1 Filter Backwash Recycling Rule FBRR Final: June 8, 2001.
Drinking Water Technical Assistance Water Treatment Plant and Distribution System KY Water and Wastewater Operators Association 57 th Annual Conference.
Stage 2 DBP Plan Workshop May 2013 Janice Thomas, CDPH Sonoma District, Drinking Water Field Operations Branch.
ENVE 201 Environmental Engineering Chemistry 1 COLOR (Chapter 13) Dr. Aslıhan Kerç.
Effective Use Of Peracetic Acid to Reduce Effluent Disinfection Byproduct in Water Resource Recovery Facilities Isaiah Shapiro, EIT Dimitri Katehis PhD,
COLOR REMOVAL Why? and How?. WHERE DOES “COLOR”COME FROM?  For the purpose of this discussion, we will stick totally to organic color, since organics.
Formation and Dissipation of Trihalomethanes during Aquifer Storage and Recovery Operations Jason Pulley City of Salem Public Works.
National Association of Water Companies October 11, 2010 Eric Burneson, Acting Deputy Director, Office of Ground Water and Drinking Water Potential Approaches.
Operational Evaluation Level Stage 2 D/DBP Rule Compliance Michael W. Deal Compliance Assurance Section Central Office Division of Drinking And Ground.
Assessing Plant DBP Performance Using the DBP-CPE Warren J. Swanson, P.E RMSAWWA/RMWEA Annual Conference Grand Junction, Colorado Schmueser gordon.
Age of Potable Water Impacts on DBP’s and Disinfection Residuals.
Buckhorn Disinfection Byproducts / Backwash Disposal Project Board of Directors Meeting June 14, 2012.
The Stage 2 Disinfection By-Products Rule DoD/EPA State Conference Compliance Track DoD/EPA State Conference Compliance Track Atlanta, GA Atlanta, GA June.
Chemical Measurements in Drinking Water: Their Use in Monitoring Disinfection and its Consequences Kusum Perera, Ph.D.
CTC 450 Review Water processing.
1. Disinfection By-Products: A Historical Perspective Effect of Early Analytical Methodology for Analyzing Trihalomethanes (THMs) –Concentrating processes?
Stage 2 Disinfectants and Disinfection Byproducts Rule Bruce Macler USEPA Region H Br Cl Bromodichloromethane.
Future Water Supply - for the Ashley Valley D. Gerard Yates Central Utah Water Conservancy District.
STAGE 2 DISINFECTION BY- PRODUCTS (DBP’S) A GUIDE TO COMPLIANCE 1.
ENCE 667 Project Performance Measurement Patuxent Water Treatment Plant Upgrade schedule analysis Presented by: Luis Rubio Isobo Tariah.
State of Alaska Implementation of MBDP Rules Carrie Bohan Environmental Program Specialist ADEC DW Program.
Evaluation of Non-Traditional Sources of Cooling Water Sujoy Roy and Michael DiFilippo Tetra Tech Inc, Lafayette, CA and MND Consulting, Berkeley, CA EPRI.
Denver Water’s Preparation for the Stage 2 Disinfectant By-Product Rule Bruce Hale (DW) Steve Lohman (DW) Arnold Strasser (DW) Edward Koval (B&V)
Disinfectants and Disinfection Byproducts Rule (Stage 1&2 DBPRs) Wyoming Potable Water Age, Lagoon Aeration and Utility Line Replacement Seminar Hosted.
Study on removal of bromate by activated carbon By Weifang Chen.
Anion Exchange for Drinking Water Treatment
NC AWWA-WEA 2015 Annual Conference Monday, November 16, 2015 The Use of Chlorine Dioxide to Reduce TOC at Davidson Water, Inc. Water Treatment Plant.
Disinfection Byproducts and Associated Challenges Resulting from Advanced Treatment Jeff Prevatt Presented by AZ Water Association New Directions in Wastewater.
Effective Removal of Total Organic Carbon (TOC) Using MIEX Ion Exchange Treatment J. Michael Barnes, PE.
Water Treatment: Disinfection Processes Current Technology vs. Alternatives.
Water Quality Facts John Shirey City Manager William Busath, P.E. Director of Utilities Pravani Vandeyar Water Quality Superintendent.
1 Highland Water District CAPITAL IMPROVEMENT PLAN.
Water Filtration Plant Improvements Project Summary
Maebh A. Grace, Mark G. Healy, Eoghan Clifford
Advanced Technologies for Attaining and Maintaining DBP Compliance
Amherst , MA, Drinking Water System Atkins Water Treatment Plant
Disinfectant & Disinfection Byproducts Control and Optimization
CTC 450 Review Water processing.
Treatment of Perchlorate in Water
Treatment – Chlorine Disinfection
Pilot testing services and a case study to reduce organics Devendra Borikar, Laura Zettler, Jeff Avedesian, Lindsay Ariss, Luc Léonard, Denis Dolbec,
Unregulated, Emerging DBPs
New Jersey Drinking Water Quality Institute Treatment Subcommittee
ENG421 (4c) – Water Quality Management
Successful Strategies for Control of DBp Formation in Arkansas
Optimizing Chlorine Flush
City of Sunrise Wastewater Reuse Program
Adapting to a New Era: Declining Flow and Deteriorating Water Quality
Regulation of Disinfection By-Products
Disinfection Byproducts (DBPs) Operational Evaluation Level (OEL)
Case Study: Lebanon Water Works
Lebanon Water Works National Optimization Goals Case Study - Meeting the Goals at the Lebanon Water Works Company Daren Thompson, MBA, MPM.
Presentation transcript:

Trihalomethanes Removal Evaluation June 26, 2019

Introduction & Purpose Background With the onset of EPA’s Stage 2 Disinfectants and Disinfection Byproducts Rule, the Town was proactive in investigating and implementing process modifications to enhance treatment efficiency and effectively reduce regulated DBPs. Motivation Although the system is in compliance with the Stage 2 rule, the potential for exceedance still exists particularly of total trihalomethanes (TTHMs) during the summer. Purpose The purpose of this work was to assist the Town to develop and evaluate alternative DBP control strategies and provide recommendations for an effective DBP control strategy. 1. The 2004-2006 modifications worked since the data demonstrates that you are in compliance. 2. But at some locations the concentration are approaching the MCL particularly of total trihalomethanes (TTHMs) during the summer season when higher TOC levels and temperatures can drive their formation. TETRA TECH

How Do DBPs Form? An unintended consequence of chemical disinfection is the formation of DBPs. Free Chlorine (Cl2) Dissolved Organics (TOC) Disinfection Byproducts (DBP’s) Temp Br Time Factors Contributing to Higher DBP Formation TETRA TECH

Types of DBPs Trihalomethanes (TTHMs) Types of TTHMs: Chloroform Dichlorobromomethane Dibromochloromethane Bromoform Maximum Contaminant Level: 80 μg/L Haloacetic Acids (HAA5) Types of HAAs: Dichloroacetic Acid Trichloroacetic Acid Chloroacetic Acid Bromoacetic Acid Dibromoacetic Acid Maximum Contaminant Level: 60 μg/L Regulatory compliance is based on a locational running annual average (LRAA). TETRA TECH

DBP Control Strategies Flushing Modified Disinfection Move Cl2 location Reduce Cl2 dose and/or time Use an alternative disinfectant Remove DBP precursors (aka TOC) Coagulation Optimization GAC Adsorption Biological Active Carbon (BAC) Ozone-BAC MIEX / Ion Exchange Membranes Remove DBP after formation Aeration Biofiltration DBPs TETRA TECH

Treatment Requirement Water Quality and Treatment Goals Constituent Goal Basis Concentration Goal Goal Achieved? Treatment Requirement TTHM 80% of MCL 64 µg/L No 40% to 50% HAA5 48 µg/L Yes Goal Met TOC Meet DBP Goals ≤ 2.0 mg/L 50% to 65% TETRA TECH

Technologies Identified & Evaluated Spray Aeration GAC/BAC Ozone BAC Ion Exchange TETRA TECH

Spray Aeration Treatment Integration TETRA TECH

Spray Aeration Treatment Overview Two Key Considerations: TTHM Speciation 1 TTHM Re-Formation 2 TETRA TECH

TTHM Speciation TETRA TECH

Spray Aeration Treatment Example 80 µg/L THM Limit TOTAL REGULATED DBPS (µg/L)  TTHM Formation WTP SITE BOUNDARY  TTHM Formation CUSTOMERS DISINFECTION CONTACT TIME (DAYS) TETRA TECH

Spray Aeration Treatment Example 80 µg/L THM Limit TTHM Removal  TOTAL REGULATED DBPS (µg/L) WTP SITE BOUNDARY CUSTOMERS DISINFECTION AERATION CONTACT TIME (DAYS) TETRA TECH

Spray Aeration Treatment Example 80 µg/L THM Limit TOTAL REGULATED DBPS (µg/L) WTP SITE BOUNDARY CUSTOMERS DISINFECTION AERATION AERATION CONTACT TIME (DAYS) TETRA TECH

GAC/BAC Treatment Integration TETRA TECH

GAC/BAC Treatment Overview Two Key Considerations: Empty Bed Contact Time 1 Carbon Change Out Frequency 2 TETRA TECH

Biologically Active Carbon (BAC) Absorption Biological Removal F E C D B A TETRA TECH

Ozone-BAC Treatment Integration TETRA TECH

Ozone-BAC Treatment Overview Two Key Considerations: Empty Bed Contact Time 1 Biodegradable TOC Fraction 2 TETRA TECH

Ion Exchange Treatment Integration TETRA TECH

Fixed Bed Ion Exchange Overview Two Key Considerations: Effectiveness 1 How Frequently Does it Have to be Regenerated 2 (1) How frequently do we have to regenerate it (2) TETRA TECH

Treatment Performance Water Quality/ Treatment DBP Precursor (i.e. TOC) Removal TTHM Reduction Goal Achieved? Spray Aeration Does not Remove TOC 20% to 40% Mostly GAC Adsorption 30% to 70% Yes BAC 25% Typical (5% to 60% Range) 8% to 50% Possibly Ozone-BAC 15% to 50% Ion Exchange 30% to 60% ≈ Make this into a decision flow chart ≈ TETRA TECH

Conceptual Cost Opinions Alternative at 2 MGD Capacity Construction Cost Opinion ($) Unit Construction Cost Opinion ($/gal) Relative Operating cost Spray Aeration System within Clearwell $770,000 $0.40/gal Minimal $$$$ Spray Aeration System within Bear Hill and Scituate Hill Tanks $1,600,000 $0.80/gal GAC/BAC Filtration $2,000,000 $1.00/gal Moderate Ion Exchange $3,900,000 $1.95/gal Ozone-BAC $5,800,000 $2.90/gal Moderate/High Based on cost curves, vendor based estimates, and experience with analogous systems. 15% Contractor Overhead & Profit, 7% General Requirements, mobilization and bonding 30% Construction Cost Contingency TETRA TECH

Recommendations Phase I: Spray Aeration Phase II: Organic Removal Perform bench-top evaluation of spray aeration. Installation of spray aeration within the clearwell. Installation of additional spray aeration at the Bear Hill and Scituate Hill tanks or proceed with Phase II. Phase II: Organic Removal Installation of organic removal technology capable of removing 50%to 65% of the combined filtered water TOC levels. Install a 1.5 to 2.0 MGD expandable to 3.0 MGD GAC or ion exchange technology. GAC could be allowed to convert into biological mode during the higher quality winter/spring months. If GAC/BAC is selected, the design could be phased to allow the subsequent installation of ozonation, if required at a later phase. Decreased your organic removal capacity with integration of aeration with GAC To reduce the operating cost of any of the phase II alternatives, you could operate the additional treatment seasonally. TETRA TECH

Q&A June 26, 2019