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The State of Water Salem, Oregon May 8, 2009 Calcite Contactors for Corrosion Control in Small Systems Rebecca Venot Staff Engineer 425.233.3310 [email protected]

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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

    [email protected]

  • The State of Water Salem, Oregon May 8, 2009

    Outline

    • Lead and copper solubility • Regulatory overview• Calcite contactor design, operation, and

    cost

  • The State of Water Salem, Oregon May 8, 2009

    Outline

    • Lead and copper solubility• Regulatory overview• Calcite contactor design, operation, and

    cost

  • The State of Water Salem, Oregon May 8, 2009

    Lead Solubility

    Minimum lead solubility

  • The State of Water Salem, Oregon May 8, 2009

    Copper Solubility

    Minimum copper solubility

  • 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

  • The State of Water Salem, Oregon May 8, 2009

    Outline

    • Lead and copper solubility • Regulatory overview• Calcite contactor design, operation, and

    cost

  • 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.

  • 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

  • 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

  • The State of Water Salem, Oregon May 8, 2009

    Outline

    • Lead and copper solubility • Regulatory overview• Calcite contactor design, operation, and

    cost

  • 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

  • The State of Water Salem, Oregon May 8, 2009

    Calcite Contactors

    1200 College St

  • 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

  • The State of Water Salem, Oregon May 8, 2009

    Contactor Decision Tree

  • The State of Water Salem, Oregon May 8, 2009

    Design Software Used to Size System and Predict Consumption Rate

  • The State of Water Salem, Oregon May 8, 2009

    Contactors

  • The State of Water Salem, Oregon May 8, 2009

    Example Project Layout & Design

  • The State of Water Salem, Oregon May 8, 2009

  • The State of Water Salem, Oregon May 8, 2009

  • 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

  • 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

  • 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

  • The State of Water Salem, Oregon May 8, 2009

    Additional Resources

    • USEPA Revised Guidance Manual for Selecting Lead and Copper Control Strategies, March 2003.

  • 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?