calcite contactors for corrosion control in small systems€¦ · limestone bed scraping/cleaning...
TRANSCRIPT
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The State of Water Salem, Oregon May 8, 2009
Calcite Contactors for Corrosion Control in Small Systems
Rebecca VenotStaff Engineer425.233.3310
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The State of Water Salem, Oregon May 8, 2009
Outline
• Lead and copper solubility • Regulatory overview• Calcite contactor design, operation, and
cost
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The State of Water Salem, Oregon May 8, 2009
Outline
• Lead and copper solubility• Regulatory overview• Calcite contactor design, operation, and
cost
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The State of Water Salem, Oregon May 8, 2009
Lead Solubility
Minimum lead solubility
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The State of Water Salem, Oregon May 8, 2009
Copper Solubility
Minimum copper solubility
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The State of Water Salem, Oregon May 8, 2009
100
10
05 6 7 8 9 10
Cor
rosi
on R
ate,
Rel
ativ
e U
nits
pH
Corrosion vs. pH
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The State of Water Salem, Oregon May 8, 2009
Outline
• Lead and copper solubility • Regulatory overview• Calcite contactor design, operation, and
cost
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The State of Water Salem, Oregon May 8, 2009
Regulatory Overview
•US EPA Lead and Copper Rule
– First published in 1991– Revised most recently
in 2004.– When action levels are
exceeded in more than 10% of sample locations, action must be taken to control corrosion.
Action Level
Lead 0.015 mg/L
Copper 1.3 mg/L
Action level based on 90th percentile of tap water samples.
Samples taken at specified number of taps in distribution system.
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The State of Water Salem, Oregon May 8, 2009
Revised Corrosion Control Guidance From USEPA
• EPA revised rule based on feedback and experience with small systems
• New procedure based on type of exceedance (lead only, copper only, or both) and raw water quality
• pH and alkalinity are used:– to determine dissolved inorganic carbonate (DIC)– Hardness data is used to determine maximum pH increase– Decision tree/flowchart is used to determine treatment
recommendation– Additional restricting factors (i.e. iron and manganese) and cost
also impact recommendation
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The State of Water Salem, Oregon May 8, 2009
Revised Corrosion Control Guidance From USEPAthat Recommends Calcite Contactors
Lead Copper pH Fe & Mn DICYes Yes
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The State of Water Salem, Oregon May 8, 2009
Outline
• Lead and copper solubility • Regulatory overview• Calcite contactor design, operation, and
cost
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The State of Water Salem, Oregon May 8, 2009
• Calcite contactors use limestone to add calcium carbonate to water, which raises pH, and adds alkalinity.
• Advantages:– Easy and safe to operate – Reduced operating cost– Self adjusts the water pH without risk of alkali overdose– Increases alkalinity – Requires minimal maintenance and operator skill – Does not require continuous feed of chemicals– Have been used in Europe and Middle East for augmenting iron removal
• Disadvantages:– Only works on certain water qualities– No precise pH control
Calcite Contactors
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The State of Water Salem, Oregon May 8, 2009
Calcite Contactors
1200 College St
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The State of Water Salem, Oregon May 8, 2009
•Parameters needed:– pH– Alkalinity– Dissolved Inorganic Carbon (DIC)– Hardness– Calcium– Iron– Manganese– Temperature– Velocity– % Calcium Carbonate – Particle Size
Contactor Design
Go into EPA’s flowcharts for treatment technology recommendation}
Refine details of contactor design
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The State of Water Salem, Oregon May 8, 2009
Contactor Decision Tree
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The State of Water Salem, Oregon May 8, 2009
Design Software Used to Size System and Predict Consumption Rate
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The State of Water Salem, Oregon May 8, 2009
Contactors
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The State of Water Salem, Oregon May 8, 2009
Example Project Layout & Design
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The State of Water Salem, Oregon May 8, 2009
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The State of Water Salem, Oregon May 8, 2009
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The State of Water Salem, Oregon May 8, 2009
Capital Cost
•“Jump” in price occurs with increase in number of tanks installed
Flow vs. Capital Cost
$0$2,000$4,000$6,000$8,000
$10,000$12,000$14,000
40 60 80 100 120 140 160
Flow (gpm)
Cap
ital C
ost (
$)
Flow vs Equipment Cost
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The State of Water Salem, Oregon May 8, 2009
Operations & Maintenance
Procedure FrequencyInspection of the tank WeeklypH monitoring to ensure target pH values are met PeriodicallyFlow adjustment to maintain constant contact time PeriodicallyLimestone bed scraping/cleaning and refilling 6-8 weeksComplete media replacement Once in 10 yearsMonitor flow to ensure it is within permissible values RegularlyHeadloss inspection WeeklyMonitor height of limestone media MonthlyEnsure no precipitates on media surface Regularly
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The State of Water Salem, Oregon May 8, 2009
Operation and Maintenance Cost
• Typically very low– Includes regular pH monitoring– Limestone addition when pH decreases
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The State of Water Salem, Oregon May 8, 2009
Additional Resources
• USEPA Revised Guidance Manual for Selecting Lead and Copper Control Strategies, March 2003.
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The State of Water Salem, Oregon May 8, 2009
Questions?
Calcite Contactors for Corrosion Control in Small SystemsOutlineOutlineLead SolubilityCopper SolubilityCorrosion vs. pHOutlineRegulatory OverviewRevised Corrosion Control Guidance From USEPARevised Corrosion Control Guidance From USEPA�that Recommends Calcite ContactorsOutlineCalcite ContactorsCalcite ContactorsSlide Number 14Contactor Decision TreeDesign Software Used to Size System and Predict Consumption RateContactorsExample Project Layout & DesignSlide Number 19Slide Number 20Capital CostOperations & MaintenanceOperation and Maintenance CostAdditional ResourcesQuestions?