aeration strategies for tthm control€¦ · aeration strategies for tthm control chad seidel,...
TRANSCRIPT
![Page 1: Aeration Strategies for TTHM Control€¦ · Aeration Strategies for TTHM Control Chad Seidel, Ph.D., P.E. Stephen Acquafredda, P.E. ... – TTHM Reformation – Bench / Pilot Scale](https://reader034.vdocuments.mx/reader034/viewer/2022042222/5ec820760fbb8862012aa4a8/html5/thumbnails/1.jpg)
Aeration Strategies for TTHM Control
Chad Seidel, Ph.D., P.E. Stephen Acquafredda, P.E.
Damon S. Williams Associates, LLC AZWA Water Treatment Committee Seminar Series
Water System Optimization Tuesday, February 23, 2010
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Presentation Outline • Background
– Stage 2 Disinfection Byproducts Rule • DBP Reduction Alternatives
• Aeration Strategies • Aeration Strategy Evaluation Tools
– Modeling – TTHM Reformation – Bench / Pilot Scale Testing
• Case Studies – Tempe, Phoenix, Mesa
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Regulatory Drivers • Stage 2 D/DBP Rule
– Compliance year: 2012 – MCL same as Stage 1 DBPR
• 0.080 mg/L TTHM (80 μg/L) • 0.060 mg/L HAA5 (60 μg/L)
– Compliance based on Locational Running Annual Average (LRAA)
• RAA for Stage 1 D/DBP Rule – Monitor sites with highest DBP concentrations
• Sites selected through Initial Distribution System Evaluation (IDSE)
– Operational Evaluation
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DBP Control Options
• Existing Facilities Optimization – Treatment Plant – Distribution System
• New Facilities Implementation
– Treatment Plant – Distribution System – Remote DBP Control
Make the most of what you’ve got!
Evaluate using lifecycle costs!
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DBP Control Options
• Treatment Plant – Enhanced Coagulation – GAC Adsorption – PAC Adsorption – MIEX Process – Advanced Oxidation
• Ozone • Chlorine Dioxide • Permanganate • UV (with peroxide or
catalyst) – River Bank Filtration – Chloramination
• Distribution System – Reduce water age – Blending with lower
TOC/DBP water – Remote DBP control
• GAC/BAC • Aeration
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WTP
Low DBP
High DBP
Implement Remote DBP Control
• Works in isolated areas of high DBPs
Remote DBP Control
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Aeration for TTHM Removal • TTHMs can be removed by
aeration/air stripping • Efficiency depends on
volatility (Henry’s Constant), which increases with temperature
• TTHM reformation after re-chlorination a concern
• Well documented process, but limited implementation for this purpose
• Aeration does not remove HAAs
Compound Formula
Henry’s Constant
(atm, 20°C)
Oxygen O2 43,000
Carbon Dioxide CO2 1,510
Chlorine Cl2 585
Chloroform CHCl3 480
Bromodichloro-methane CHCl2Br 118
Dibromochloro-methane CHClBr2 47
Bromoform CHBr3 35
Ammonia NH3 0.76
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Aeration Strategies • In-reservoir Aeration Strategies
– Bubble Aeration
– Spray Aeration
– Surface Aeration
• External Aeration Strategies – Tray / Packed Tower
– Spray / Bubble Vessel
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• TTHM reduction and energy use dependent upon A/W ratio
• Considerations: – Blower passes air through distributor
• Distributor installed within reservoir • Liner penetrations require repair
– Orifice / nozzle clogging – Blower maintenance – Intake air filter change out
Bubble Aeration Technology Assessment
“The poor economy of the diffused aeration process for THM removal can be explained by the rapid saturation of air bubbles with THMs as the bubbles rise through the column.” Roberts and Levy, JAWWA 1985
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0%
10%
20%
30%
40%
50%
60%
70%
80%
90%
0 5 10 15 20
A/W Ratio
% R
emov
al
$- $10,000 $20,000 $30,000Annual Energy Cost
Chloroform Bromodichloromethane DibromochloromethaneBromoform TTHM
Assumptions:TTHM = 102 ug/LCHCl3 = 48.5 ug/LCHCl2Br = 32.0 ug/LCHClBr2 = 19.2 ug/LCHBr3 = 2.3 ug/L
Daily Outflow = 0.68 MGDRes. Retention Time = 29 hrWater Depth = 4 mBlower Efficiency = 40%Electricity Cost = $0.08/kWh
Bubble Aeration Model Estimates
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• Pump flow from reservoir outlet through hub & lateral system
• Maximum flow evaluation – Spray area for each nozzle / orifice – Flow rate per nozzle / orifice
• Considerations: – Can use reservoir inflow pressure, if available,
for potential energy savings – Structural support of piping – Distributor system installed within reservoir – Can reservoir be shutdown / drained? – Liner penetrations require repair – Orifice / nozzle clogging
Spray Aeration Technology Assessment
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• Surface aerators float at water surface • Maximum flow evaluation
– Determine area of influence per unit – TTHM reduction dependent upon unit
power input (W/m3) • Considerations:
– Equipment must be supported in place – NSF approved equipment
• Limited application in drinking water – Reservoir access to each aeration unit
Surface Aeration Technology Assessment
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Surface Aeration Model Estimates
0%
10%
20%
30%
40%
50%
60%
70%
80%
90%
100%
0 0.5 1 1.5 2 2.5 3 3.5 4 4.5 5
Power Input (W/m3)
% R
emov
al
$0 $5,000 $10,000 $15,000 $20,000 $25,000
Annual Energy Cost
Chloroform Bromodichloromethane DibromochloromethaneBromoform TTHM
Assumptions:TTHM = 102 ug/LCHCl3 = 48.5 ug/LCHCl2Br = 32.0 ug/LCHClBr2 = 19.2 ug/LCHBr3 = 2.3 ug/L
Daily Outflow = 0.68 MGDRes. Retention Time = 29 hrAerator Motor Efficiency = 40%Electricity Cost = $0.08/kWh
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• Tray tower flow rates up to around 1,000 gpm
• Considerations: – Additional footprint required – Minimal service & equipment interruption
for installation & maintenance – Maintenance may include removal of
scaling from trays on regular intervals – Automation required to control flow rate to
tray tower system
Tray Tower Aeration Technology Assessment
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Aeration Strategy Evaluation Tools
• Aeration Modeling – Aeration System Analysis Program (ASAP)
• Bubble • Surface
– Spray aeration spreadsheet tool • Based on AWWA Water Quality Treatment
Handbook 5th edition
– Tray tower TTHM reduction • Based on WaterRF Project No. 3103 Localized
Treatment of Disinfection By-Products, Las Vegas Valley Water District, South Central Connecticut Regional Water Authority, and City of Phoenix Water Services Department, 2009
ASAP
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DBP Formation Potential Factors: USEPA WTP Model Form
– DBP = TTHM or HAA5 (μg/L) – TOC = Treated Water TOC (mg/L) – UVA = Treated Water UVA (1/cm) – Cl2 = Applied Chlorine Dose (mg/L) – Br- = Treated Water Bromide (μg/L) – T = Temperature (°C) – pH = Treated Water pH – t = Reaction Time or Water Age (hours) – A = Base Coefficient – a,b,c,d = Exponent Coefficients – α = Temperature Coefficient – β = pH Adjustment Coefficient
Simulated Distribution System (SDS) tests used to
validate model predictions
dpHTcba tBrClUVATOCADBP )(*)(*)(*)(*)(*)*( )5.7()20(2
−−−= βα
(Solarik et al., 1999)
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Arizona Case Studies • City of Tempe, AZ
• City of Phoenix, AZ
• City of Mesa, AZ
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City of Tempe, AZ
• Evaluation: Surface water treatment plant 12 MG reservoir
• Methods evaluated – Groundwater Blending – Coagulation / Enhanced Coagulation – Aeration
• Bubble (modeling & bench testing @ A/W=15) • Spray (modeling & bench testing) • Surface (modeling) • TTHM Reformation (modeling & SDS tests)
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Baseline SDS Test
0
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-24 0 24 48 72 96 120
Elapsed Time (hr)
pH a
nd T
empe
ratu
re
0
0.2
0.4
0.6
0.8
1
1.2
1.4
1.6
1.8
2
Chlo
rine
Resi
dual
pH: Temperature (ºC): Chlorine Residual (mg/L):
Aeration followed by rechlorination
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Baseline & Bubble Aeration SDS Test
0
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40
60
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120
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160
-24 0 24 48 72 96 120
Elapsed Time (hr)
TTHM
(ug/
L)
Baseline SDS Post Aeration Rechlorination SDS
TTHM Removal: 48.6 ug/L – 21.8 ug/L = 26.8 ug/L = 55% Removal Model Prediction ~ 56% Removal
Aeration followed by rechlorination
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City of Tempe, AZ
• Bubble aeration capital and O&M costs higher than spray or surface aeration – Bubble aeration achieved greatest TTHM reduction
given physical constraints • Long residence time in distribution system post-
aeration limited DBP control effectiveness
Parameter Target Bubble Spray Surface
Average Flow rate, mgd 24 Reservoir Max Level, ft 18 % TTHM Reduction 35% 23% 8% 10%
Energy Use (kWh/yr) N/A 7,884K 1,144K 1,769K
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City of Phoenix, AZ • Evaluation: Distribution system 2 MG
reservoir – Criteria: TTHM reduction, lifecycle cost,
constructability, ease of operation, impact on operation, required time out of service, mixing
• Aeration methods evaluated – Bubble (modeling @ A/W ~ 6) – Spray (modeling) – Surface (modeling) – External Methods (testing & vendor coordination)
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City of Phoenix, AZ
• Surface aeration capital and O&M costs lower than for other strategies
• Non-cost surface aeration advantages – Equipment maintenance with minimal impact on
reservoir operation
Parameter Tray Bubble Spray Surface
Average Flow rate, mgd
0.7
Reservoir Max Level, ft 25
% TTHM Reduction 30%
Energy Use (kWh/yr) 210K 196K 299K 49K
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City of Mesa, AZ • Evaluation: Multiple distribution system
reservoirs including 0.5 & 0.1 MG shown
• Aeration methods evaluated – Bubble (modeling @ A/W ~ 6) – Spray (modeling) – Surface (modeling)
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City of Mesa, AZ
Parameter Target Bubble Spray Surface Average Flow rate, mgd 0.5 Reservoir Max Level, ft 10 % TTHM Reduction 15% 55% 22% 60% Energy Use (kWh/yr) N/A 98K 65K 49K
• Surface and spray aeration had low capital and O&M costs
• Spray aeration becomes competitive when target TTHM reduction is low
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Impact on Chlorine Residual
• Predominant chlorine species in water around neutral pH are HOCl and OCl- – Species are less volatile than Cl2
• Literature and recent testing have mixed results – Some show no chlorine residual loss – Some show up to 40% chlorine residual loss
• All aeration strategies should include chlorine residual maintenance facilities
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Conclusions • In-reservoir aeration is an efficient strategy to
reduce TTHMs in terms of capital and annual operating costs – Target high TTHM water at remote storage
facilities • Modeling shows surface aeration has the
lowest capital & operating cost – Limited application in drinking water
• NSF certification required for equipment – Application not appropriate for some reservoirs
• Use available literature and models to compare aeration strategies and determine best solution
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Contact Information • Chad Seidel, Ph.D., P.E.
Damon S. Williams Associates, L.L.C. 1624 Market Street, Suite 475 Denver, CO 80202 Phone: (303) 989-2205 [email protected]
• Stephen Acquafredda, P.E. Damon S. Williams Associates, L.L.C. 2355 East Camelback, Suite 700 Phoenix, AZ 85016 Phone: (602) 265-5400 [email protected]