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Trihalomethanes Removal Evaluation

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Presentation on theme: "Trihalomethanes Removal Evaluation"— Presentation transcript:

1 Trihalomethanes Removal Evaluation
June 26, 2019

2 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 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

3 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

4 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

5 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

6 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

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

8 Spray Aeration Treatment Integration
TETRA TECH

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

10 TTHM Speciation TETRA TECH

11 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

12 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

13 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

14 GAC/BAC Treatment Integration
TETRA TECH

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

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

17 Ozone-BAC Treatment Integration
TETRA TECH

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

19 Ion Exchange Treatment Integration
TETRA TECH

20 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

21 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

22 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

23 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

24 Q&A June 26, 2019


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