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    Corrpro. All Rights Reserved.

    Corrosion Technologies to Assessthe Condition of Force Mains

    James T LaryCorrpro

    1055 W Smith RoadMedina, OH 44256Tel: 330-723-5082

    Email: [email protected]

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    Practical

    Tendency of a Metal to Revert

    to its Native State

    Scientific

    Electrochemical Degradation

    of Metal as a Result of a Reaction

    with its Environment

    Corro sion Can be Defined as Either:

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    IRON OXIDE REFINING MILLING

    IRON,STEEL,PCCP CORROSION IRON OXIDE

    Corrosion Process

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    External Corrosion Attack

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    Temporary Fix ?

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    Anodic Area

    Internal & External Corro sion

    of Force Mains.

    Solids

    Buildup

    H2S

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    24 DIP

    Multiple failures onbottom of pipe

    Performed ultrasonic

    thickness measurements

    Scouring and turbulentflow contributed to failure

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    24 Ductile Iron Force Main

    Internal failure following

    loss of internal mortar

    lining

    Failure was along top ofpipe due to formation of

    hydrogen sulfide gas

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    24 DIP & Steel

    Internal pipe failuresalong crown of pipe

    Failures following loss of

    internal mortar lining

    Cause is formation ofhydrogen sulfide gas

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    Dual 26 Force Mains

    Internal failures at

    bottom of pipe

    Failure following loss of

    internal mortar lining

    Failures concentrated at

    low areas (dips) in

    pipeline alignment

    Cause is corrosion under

    accumulated solids

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    36 Above Ground Crossing

    Failure of force mainat above ground crossing

    Crown of pipe attacked

    by hydrogen sulfide gas also

    external corrosion of pipe

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    History of Iron Pipe

    Cast Iron

    - Introduced to North America during the 1800s and

    installed till the 1970s.

    - Early on, statically cast process produced a thick

    walled, heavy pipe.

    - No longer produced in North America.

    Ductile Iron

    - Introduced in 1955 as an

    improvement to cast iron.

    - Centrifugal castingprocess produces a thinner

    walled, lighter pipe which is

    stronger and more ductile

    than cast iron.

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    Actual size of AWWA Specification Thickness Reductions

    for 36-inch Diameter Cast and Ductile Iron Pipe - 1908 to Present

    (150 PSI Operating pressure)

    1.58 in.

    1908 1952 1957 1957 1976 1985 1991 Less

    CLD CL 150 CL 23 CL 22 CL 3 CL 50 CL 150 Tolerances

    CI CI 18/40 21/45 DI DI DI

    CI CI

    1.22 in.

    0.94 in.

    0.87 in.

    0.58 in. 0.43 in.0.38 in.

    0.21 in.

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    Cast (Grey) Iron

    Failures

    Cast Iron Pipe

    (thicker walled pipe)

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    Ductile Iron

    External pitting

    (concentrated) corrosion

    attack on thinner walled

    ductile iron pipe.

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    Adverse Cond it ion s fo r Metal l ic Pipe

    - High Chlor ides- Low Soi l /Water Resist iv i ty

    - High Sulfates

    - Acidic Soi ls

    - Wet/Dry Fluctuations

    - Bimetall ic Coupl ings

    - Stray Current Interference

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    Stray Currents

    Underground Gas &

    Oil Piping AC Transmission Lines

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    Pipe

    Metallic Coupling

    Lower Stress Area(Cathode)

    Threaded Bolt

    Higher Stress Area

    (Anode)

    Stress Corrosion

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    The rate and magnitude of corrosion depends

    on a number of factors:

    Pipe Material and Characteristics

    Operating Conditions

    Construction Methods

    Environment (age not a good primary metric)

    Internal / External Corrosion Attack

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    #2Indirect Inspection

    #3Direct Examination

    #1Pre Assessment

    #4Post Assessment

    Initial development driven

    by federally regulated

    pipeline integrity rules

    Methodology also quite

    applicable to water /

    wastewater

    Pipeline Condi t ion Assessment Process

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    #1 Pre-Assessment:

    Define pipe segments by

    construction contracts and similar

    characteristics, e.g. material,

    construction practices

    Identify specific locations along

    the pipeline

    Air Release Points/Man ways Pipeline crossings

    Known area where piping

    failures have occurred

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    Good listening operating history,criticality, consequences of failure

    Leak & Repair Records

    Pipe Bone Yard

    Coordination of ConditionAssessment Efforts With OtherActivities Excavations

    Repairs

    Project construction drawings andspecifications (High and low points)

    Pipe materials and characteristics Wall thickness

    Pressure rating

    Flow Rates

    Air Release points/operational status Coatings and Linings

    Bedding and backfill material

    As-built documentation

    Soil corrosivity, e.g. resistivity, pH,chlorides, moisture

    Adjacent utilities and crossings

    Sources of stray current corrosion Nearby cathodic protection systems

    Direct current powered transit systems

    High voltage overhead AC power lines

    #1 -Pre-Assessm ent Data Gathering & Plann ing :

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    Indirect Inspection techniques:

    In-Situ Soil Resistivity Measurements

    Soil Sample Collection and Analysis

    Ultrasonic Thickness Measurements (air releasevalves or accessible points)

    Direct Examination of Exposed Pipe Sections

    Stray Current Evaluations

    #2 - Ind irect Inspec tion :

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    #2 - Ind irect Inspec tion :

    Integrate all data along pipeline alignment

    Analyze Data and Rank Indications: Severe Moderate

    Minor

    Select at sites for direct inspectionlocations shouldbe where corrosion activity is most likely

    Select control site where corrosion activity is the leastlikely

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    #3 - Direc t Exam ination

    Excavating the pipe

    Performing physical

    inspection & photograph

    Evaluating integrity of

    coating/wrap, if present

    Testing the pipe surface,e.g. corrosion pitting

    UT measurements

    Measuring dimensions of

    corrosion defects

    Analyzing surrounding soil/ groundwater

    Internal video/inspection

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    Inspector name_________ Date____ Address of pipeline inspection ________________ Leak? Yes____ No____ File Number:_____________

    1) Type of Pipe: cast iron_____ ductile iron____ carbon steel___ copper______ carbon steel_____ non metallic_____ concrete________other____

    2) Diameter of pipe _____ Pipeline Name_________ Service Type: Water____ Wastewater____ Estimated date of pipe installation______ Depth of pipe______3) Type of Pipe: Distribution____ Transmission____ Service_____ Hydrant _____ Mechanical joint_____ Fasteners____ _ Other____ Unknown____

    4) Type of Coating: Polyethylene Encased____ Shop applied coating___ No Coating____ Tape Wrap____ Unable to determine____

    5) External Pipe Condition: Very Good____ Good____ Poor____ comments:____________________________________________________________________

    ___________________________________________________________________________________________________________________________________________

    6) Ultrasonic Thickness Measurements and comment______________________________ Internal Lining Present _____ Yes ____No comment_________________

    6) Is corrosion pitting evident? ____ Yes ____ No Number of Pits______ Typical Size of Pits______ Quantity of pits:______

    7) Is graphitization evident (longitudinal or circumferential breaks) ____Yes ____ No

    8) Is the pipe installed in (check off appropriate items): Industrial area____ Residential area____ Rural area____ Near street or road ____Near creek or waterway ____ In reclaimed land___ Near oil or gas pipelines____ Near high voltage lines ____.

    8) Describe soil conditions where inspection occurred: wet____ dry____ clay soil ____ rocky soil____ cinders ____ other____________________

    9) Where soil samples obtained, sealed and analyzed for chlorides, moisture content, pH, sulfides, resistivity? If yes resul ts were: _____________________________

    10) Were previous repairs made on the pipeline (leak clamps, etc) Yes____ No ____. Was new pipe installed____ Yes ____ No.

    11) Was a repair clamp installed on the pipe during inspection ___ Yes ___ No

    12) Was a galvanic anode installed as part of the inspection process? ___ Yes ___ No, if yes size and quantity

    13) Please relay additional comments:

    _____________________________________________________________________________________________________________________________________

    __________________________________________________________________________________________________________________________________________________________________________________________________________________________________________________________________________

    14) Plan of Action____________________________

    15) Insert digital photos below:

    Force Main Pipeline Inspection Report

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    #3 - Direc tExaminat ion:

    When corrosion is found, perform

    a root cause analysis

    Implement localized corrosion

    protection

    Install instrumented test station

    for future assessment of

    corrosion activity, e.g. corrosion

    rate probes

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    #4 Post Assessment:

    Calculate remaining life

    Pit growth rate and wallthickness

    Internal or External Corrosion

    Coupons

    Electrical resistance (ER)probes

    Maximize benefit by

    Capture ideas for improvement

    Determine need/timeframe forupdate evaluations

    Identify corrective actionoptions

    Probe-Tag: 5500 K11A-1

    Probe Type: PA-0.4-10-0.1-6Probe serial No.: PA04270025

    Test initiated: 20-12-2005

    0

    100

    200

    300

    400

    500

    600

    700

    800

    900

    1000

    1 7/03 /0 6 1 8/03 /0 6 1 9/03 /0 6 2 0/03 /0 6 2 1/03 /0 6 2 2/03 /0 6 2 3/03 /0 6 2 4/03 /0 6 2 5/03 /0 6

    Date

    AC

    current-

    A/m2

    Corrosionratemicron/y

    -80

    -70

    -60

    -50

    -40

    -30

    -20

    -10

    0

    10

    20

    JDC

    A/m2

    Uac(V)

    Corrosion rate Uac Jdc

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    #4 Post Assessment Recommendations:

    Identify Corrective Options

    Operational Procedures

    Treatment Practices

    Internal Lining

    Cathodic Protection

    Stray Current Mitigation Partial or Full Pipeline

    Replacement

    Pipeline Monitoring

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    Program fo r Exist ing MainsBreak Reduct ion L ife Extension Through Cathodic Protect ion

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    Pipe

    Metallic Coupling

    GalvanicAnode

    Anode Lead Wire Connection

    Cathodic Protection of Metallic Fitting

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    Meter Vaults

    (Keep dry if possible)

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    Other Structures

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    Summary

    Effective management of force mains pipeline includesunderstanding and managing the risk of corrosion

    A systematic approach to condition assessments results

    in the most value at the lowest cost

    Retrofitting with accepted industry practice such as

    internal linings, treatment programs, operational

    adjustments, or cathodic protection may be a cost

    effective options for extending the life of existing mains

    A key asset management strategy is to include suitable

    corrosion control in the design of new force mains

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    Thank You

    James T Lary

    (330) 241-6615

    [email protected]