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ASTS Liabilities

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    Liabilities to AssetsLiabilities to Assets

    Presented by:Presented by:

    Eric BonnerEric Bonner

    Corrpro Companies, inc.Corrpro Companies, inc.Atlanta, GeorgiaAtlanta, Georgia

    [email protected]

    @corrpro.com

    (678) 848-0688(678) 848-0688

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    IRON OXIDE REFINING MILLING

    STEEL CORROSION IRON OXIDE

    THE PROBLEMTHE PROBLEM....

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    Why Provide Corrosion Control?

    Regulatory Compliance

    Preserve Assets That Have Become

    LIABILITIES!

    Dramatically Reduce Likelihood of

    Product Releases

    Significantly Reduce Maintenance Costs

    Environmental Preservation

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    Anodic Area

    -600mVCathodic Area

    -550mV

    SAND

    CURRENT FLOW

    External Corrosion of

    Tank Bottom

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    SANDCURRENT FLOW

    Corrosion Cell Caused

    by Foreign Material in

    Sand Cushion

    CLAY

    Steel Tank Floor

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    New Bottom (Anode)

    CURRENT FLOW

    SAND

    SAND

    New Steel Coupled to Old Steel

    Old Bottom (Cathode)

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    DRY

    SAND

    MOIST SAND

    WATER

    Corrosion Caused by

    Poor Water Drainage

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    - Approximately 25% of States now- Approximately 25% of States now

    require cathodic protection be installedrequire cathodic protection be installed

    and maintained on new, refurbished, orand maintained on new, refurbished, or

    repaired tanks in contact with soil orrepaired tanks in contact with soil orsand foundations.sand foundations.

    - A number of other states are in the- A number of other states are in the

    process of implementing regulationsprocess of implementing regulationsgoverning ASTgoverning ASTs.s.

    State Level

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    MAJOR OIL

    Vast Majority of Oil Marketers Have

    Employed CP for Decades

    Laws Changing Dramatically

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    Types of Cathodic Protection

    GalvanicGalvanic: Current obtained from a metal: Current obtained from a metalwith a higher energy level. with a higher energy level.

    Impressed CurrentImpressed Current : Requires external: Requires externalpower source (transformer power source (transformer

    rectifier). rectifier).

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    Structure

    MagnesiumAnode

    Current Flow

    Galvanic Cathodic Protection

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    Test

    Box

    Anode

    Cells

    Tank

    Galvanic Anodes

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    SAND QUALITY

    The rate of corrosion is dependent on the

    characteristics of the sand.

    The 1stmeans of corrosion control is a

    good quality sand material.

    On-site testing has indicated that

    provided sand is as much as ten timesmore corrosive than recommended sand.

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    Sand Recommendation

    Silica

    pH Between 6.5 and 8.5

    Moisture less than 5%

    Chlorides less than 10 ppm

    Resistivity greater than 30,000 ohm-cm

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    Rectifier

    Anode

    Groundbed

    ( - ) ( + )

    Pipeline

    (Structure)

    Current

    Flow

    Impressed Current System

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    Above Ground Storage Tank Vertical ImpressedAbove Ground Storage Tank Vertical Impressed

    Current Anodes - Existing TanksCurrent Anodes - Existing Tanks

    Sand

    Anodes

    Rectifier

    NegativeConnection

    +

    -

    Concrete

    Ringwall

    Tank

    AnodesRectifier

    -

    +

    Negative

    Connection

    Tank

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    Shallow Anodes

    Tank

    Rectifier

    (-)

    (+)

    Anode

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    Anodes

    Junction

    Box

    Rectifier

    -+

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    Deep Anode

    Tank

    (+)

    (-)

    RectifierTank

    Tank Tank

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    MFLMFL FloorFloorInspectionInspection

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    Mechanical Integrity

    API-653 Inspections Should CoincideWith the Results of a CP SystemEvaluation

    Corrosion Engineers and MechanicalInspectors Must be on the Same Page

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    Tank

    Rim Potential Measurements

    Portable Reference Cell

    Soil

    (+)

    ????

    -850mV-850mV

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    Rim 25' Center 55' Rim

    On -1411 -698 -404 -601 -1455

    Off -902 -664 -402 -578 -911

    Reference Cell

    Bullseye

    Monitoring

    Tube

    Test /

    Access

    Station

    boveground

    orage Tank

    de

    3Typical

    Potentials (mV)

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    Directional Boring Under

    Existing AST

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    2 !PVC

    Grade

    Aboveground

    Storage Tank

    3

    Typical

    Test/Access

    Station

    Monitoring

    Tube

    REFERENCE CELL MONITORING TUBEREFERENCE CELL MONITORING TUBE

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    Directional Bore Under Tank for Anode or

    Reference Cell Placement

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    ABOVEGROUND STORAGE TANK

    CATHODIC PROTECTION

    3!PVC 20%Exposure

    Anode Material

    Anode Tube

    10

    Typical

    Test/Acces

    s Station

    Grade

    Aboveground

    Storage Tank

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    Computer Guided Horizontally

    Bored Anode System

    Tank

    Rectifier

    (+)

    (-)

    Anode

    Splice Box

    Anode

    Pipe

    Monitoring

    Pipe

    Anode Pipe

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    CP Applications for Re-bottomed orCP Applications for Re-bottomed or

    New TanksNew Tanks

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    New Floor Installation on Existing ASTNew Floor Installation on Existing AST

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    Anode

    Reference

    Cells

    Tank

    Impressed Current

    Junction

    Box

    (-)

    (+)

    Rectifier

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    CP Installation on Rebottomed TankCP Installation on Rebottomed Tank

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    Above Ground

    Storage Tank Bottoms

    with Secondary Containment

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    New Tank Construction with LinerNew Tank Construction with Liner

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    Anode & Reference Cell PlacementAnode & Reference Cell Placement

    in High Resistance Sandin High Resistance Sand

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    Liner

    Floor

    AnodeConduit

    CP Installation on Double Bottom TankCP Installation on Double Bottom Tank

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    Installation of CP System onInstallation of CP System on

    Lifted ASTLifted AST

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    Explosion Proof Unit

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    Reference Cell Placement Under Tank Bottom

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    Inspection of CP SystemInspection of CP System

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    -Record Volts/Amps

    -Compare values to target settings

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    Cathodic Protection Monitoring

    Read rectifiers every 60 days.

    Conduct annual inspection (obtainpotentials) by NACE certified

    individuals.

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    Annual Cathodic Protection Survey

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    Internal Corrosion

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    Anode Cathode

    Water / Sediment

    Fuel Product

    Internal Corrosion

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    CoatingAnode

    Bolt

    Tank Bottom

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    Hot Asphalt Tank Bottoms (require special CP

    design considerations due to heat)

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    Recommended Practices

    API-651 - Cathodic Protection of Aboveground Petroleum

    Storage Tanks:

    NACE RP0193-2001 - External Cathodic Protection of On-

    Grade Carbon Steel Tank Bottoms:

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    Recommended Practices

    API-651 - Cathodic Protection of Aboveground Petroleum

    Storage Tanks:

    Galvanic anodes method is not practical for

    protection of large bare structures.

    NACE RP0193-2001 - External Cathodic Protection of On-

    Grade Carbon Steel Storage Tank Bottoms:

    Galvanic protection systems can be applied to

    tank bottoms where the metallic surface areaexposed to the electrolyte can be minimized

    through the application of a dielectric coating or the

    area is small due to the tank size or configuration.

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    SummarySummary

    - Be aware of all regulations that may

    pertain to your tanks and piping. When in

    doubt talk to the governing agencies.

    - Engage NACE qualified & experienced

    personnel to engineer/maintain your

    cathodic protection system.

    - Refer to NACE/API Standards for guidance.

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    QuestionsQuestions

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    Thank YouThank You

    Eric BonnerEric Bonner

    Corrpro Companies, Inc.Corrpro Companies, Inc.

    Atlanta Regional OfficeAtlanta Regional Office

    Office (770) 761-5400Office (770) 761-5400Mobile (678) 848-0688Mobile (678) 848-0688

    [email protected]@corrpro.com


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