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    Pipe Line

    Corrosion

    Cathodic

    Protection

    THIRD

    EDITION

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    Gulf

    Professional Publishing

    an imprint of

    But terworth-Heinem ann

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    PipeLine

    Corrosion

    ^ ^and ^

    Cathodic

    Protection

    A

    practical manual

    lor

    corrosion engineers,

    technicians, and

    field

    personnel

    THIRD

    EDITION

    MarshallE.Parker

    Edward G.Peattie

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    Gulf

    Professional Publishing

    and Butterworth-Heinem ann are

    imp rints

    of

    ElsevierScience.

    Copyright

    1999

    by

    Elsevier Science (USA).

    All

    rights

    reserved.

    Originally

    published

    b y

    G ulf Publishing Compa ny, Houston,

    TX.

    No part

    of

    this publication

    may be

    reprodu ced, stored

    in a

    retrieval system,

    or

    transmitted in any

    form

    or by anymeans, electronic, m echa nical,

    photocopying, recording, or otherwise, w itho ut the prior written perm ission of

    the

    publisher.

    Permissions m ay be sought directlyfromElsevier's Science & Technology

    Rights Department

    inOxford, UK:

    phon e: (+44) 1865

    843830,

    fa x: (+44)

    1865

    853333,

    e-mail: p [email protected]. Y ou m ay also complete

    your request on-line via the Elsevier Science ho me page

    (http://www.elsevier.com), by selecting 'CustomerSupport'and then

    'Obtaining

    Permissions'.

    This book is printed on acid-free pape r.

    Libraryof C ongressCataloging-in-Publ icationData

    Parker, M arshall E.

    Pipe line corrosion and cathodic protection.

    Includes index.

    ISBN

    0-87201-149-6

    1.

    PipelinesCorrosion

    2.

    Pipel inesCathodic

    protection.

    I.

    Peattie,

    EdwardG. II.Title

    TJ930.P33 1984

    621.8'672

    83-22630

    The publisher offers special discounts on bulk orders of th is book.

    For information,pleasecontact:

    Managero fSpecialSales

    Elsevier Science

    200

    Wheeler Ro ad

    Burlington,

    MA01803

    Tel:781-313-4700

    Fax:781-313-4802

    For

    information

    on all

    Gulf

    publications

    available, contact

    our

    World Wide

    W eb

    hom epage at

    http://www.bh.com/gulf

    10

    9 8 7 6

    Printedin theU nited Stateso fAmerica.

    iv

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    C o n t e n t s

    Preface to Third Edition vii

    Preface to

    First

    Edition ix

    1

    Soil Resistivity Su rveys

    1

    Soil ResistivityUnits. Two -Terminal Resistivity Determina tion. Four-

    Terminal

    Resistivity Determination. Other Methods. Locating

    H ot

    Spots on Bare Lines. Surveys fo r Ground Beds. Area Surveys. Loga-

    rithmic Resistivity Ranges. Sum m ary.

    2 Potential Surveys 16

    Pipe-to-Soil Potentials: Electrodes. Electrode Placement. Pipe Line

    Connection. Surface Potential Survey

    fo rCorrosion. Pipe-to-Soil Po-

    tential as a Criterion of Cathodic Protection. Other Applications of

    Pipe-to-Soil Potentials. Other Criteria. Summary.

    3

    Line Currents

    31

    Measurement of Line Current in Test Section. Stray-Current Studies.

    Long-Line

    Currents. Cathodic Protection Tests. Coating Conductance

    Measurement. Summary.

    4

    Current Requ irement Surveys

    36

    The Problem: Coated Lines. Principles ofC urren t RequirementTest.

    Current

    Sources

    for

    Tests. Temporary Ground Beds. Special Condi-

    tions. Summary.

    5 Rectifier Systems forCoated Lines 45

    General Design Principles. A ttenu ation Curves. LineTermination. An-

    odeProxim ityEffects. Atte nu atio n w ith M ultiple Drain Points. Design

    Procedure. An Alternate Method. The Economic Balance. Summary.

    v

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    6

    Ground

    BedDesignand Installation 59

    Design Principles. D isturb ing Factors. Field M od ification . Installatio n

    Methods. H igh-Sil icon Iron Anod es. Steel An odes. H orizontal G raph -

    ite Anodes.

    Deep

    Anodes. A Typical G round B ed Instal la t ion . Sum -

    mary.

    7 G alvanic Anodeson Coated Lines 78

    When

    and Where to Use Magn esium . W hen and W here to Use Zinc.

    General System Design. Insta llation Procedure. Polarization and Final

    Adjustment.

    M odif icat ion of

    Process with

    Experience. Sample Prob-

    lems. Summary.

    8 HotSpot Protection 88

    What Hot

    Spots

    Are.Hot Spot Protection. LocatingHotSpots.An-

    ode Selection and Spa cing. Field In stallatio n. Field D esign. Zinc An-

    odesin HotSpot Protection. Installation Details. Su pervisionandCon-

    trol . Summary.

    9 Stray-Cu rrent E lectrolysis 1

    Stray CurrentCorrosion. Sources of Stray Cu rren ts. Detection of Stray

    Curren t . Remedial Measures. Negat ive Bu s Bon ding. Exposure Areas.

    Potential Surveys. Secondary Exposure. Summary.

    10

    Interference

    in Cathodic

    Protection

    109

    The Problem. Basic Solutions. Design. Crossing Bonds. Calculation of

    Bond Resistance. M ult iple Bo nds.

    Auxi l ia ry

    Drainage. Parallel Lines.

    Radial-Flow Interference. Foreign Lines w ith Insu latin g Join ts. Sum -

    mary .

    11 Operation

    and

    Maintenance

    125

    ImportanceofAdequate Su pervision. Fai luresin Rect i f ier-GroundB ed

    Systems.

    Failures

    in

    Ma gnesium Anode Systems. M inim um Inspection

    Schedule

    for

    Rect i fier System. M inim um Inspect ion Schedule

    for An-

    odes. Monitor System.

    Troubleshooting.

    S u m m a ry .

    12 Coating InspectionandTesting 136

    Construction

    Inspect ion. Evaluat ion

    of

    Coat ing

    in

    Place. Coating

    or

    Leakage Conductance. Pearson Surveys. Accelerated Coating Tests.

    Summary.

    Appendix

    A

    Fundam entals

    of

    Corrosion

    146

    Appendix B Cathodic Protection of Steel inSoil 150

    Appendix

    C

    Corrosion

    of

    Steel

    in

    Soil

    153

    Appendix D Attenuation Eq uations 160

    Index 163

    vi

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    P r e f a c e to T h i r d E d i t i o n

    A pipe line buried in the earth represents achallenge. It is made of

    steela strong,but chemicallyunstable, ma terial and isplaced in an

    environment

    which

    is

    nonuniform, nonprotective,

    and

    n onyielding.

    It is

    the

    duty

    of the

    corrosion engineer

    to

    study

    the

    properties

    of

    th is system

    to ensure that the pipe line will not deteriorate.

    In 1955, when I was first working on cathodic protection fo r pipe

    lines

    in

    Saudi Arabia,

    the

    firstedition

    of

    this

    bookby

    Marshall Parker

    was jus t a year old. Fortunately, the company library contained M r.

    Parker's book. I found its simplicity and directness preferable in ap-

    proaching a

    complex subject.

    During

    the 30

    years since

    its

    p ublica tion, generations

    of

    pipe line

    en-

    gineers and technicians have used this book as their first exposure to

    corrosion control. M an y bookson thesubject have been pu blished since

    1954,but theParker book isstillthe best introductionto the fundamen-

    tals. Newtechnologyhasbeen developed, yet theprinciplesofcathodic

    protection

    are

    still

    th e

    same.

    The

    result

    is

    that

    we

    have more sophisti-

    cated

    instrum ents

    to

    use,

    bu t the

    measurements have

    not changed.

    Con-

    sequently,Ihave retained thestill-valid m aterialo f theoriginal Marshall

    text

    and

    m ade changes o nly whe n better

    and

    shorter methods

    are

    avail-

    able.

    The

    first task

    of the

    pipe line corrosion engineer

    is to

    study

    the

    prop-

    erties

    of the

    earthen environment. First,

    we

    shall learn

    how to

    measure

    th e

    re sistivity

    of the

    soil

    as a

    prepa ration

    fo r

    further

    work.

    In the

    second

    vii

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    chapter we shall study another electrical measurement: potential differ-

    ence.

    To do

    this,

    we

    shall learn about

    the

    standard electrode

    for

    this

    measurement. In Chapter 3 we go on to line currents and extend these

    measurements to current requirement surveys in Chapter 4. Thus, the

    current

    necessary

    to design a cathodic protection

    system will

    be

    calcu-

    lated.

    Chapters5 and 6showthecomputations requiredfor thedesignof an

    impressed current cathodic protection system. Then, Chapter

    7

    shows

    the

    designprocedure

    for a

    sacrificial cathodic protection system.

    The

    problem

    of

    partial cathodic protection

    of a

    pipe line

    by

    concen-

    trating

    on

    hot spots

    is

    discussed

    in

    Chapter

    8. A

    problem

    in

    Chapter

    9,

    which

    doesnot

    usually occur nowadays,

    is

    that

    of

    stray-current cor-

    rosion; however,

    a

    corrosion engineer should still

    be

    able

    toidentify

    this

    phenomenon and

    find

    its

    source.

    Interference (Chapter 10) is a problem

    corrosion engineers face every

    day and are

    still learning about.

    The last two chapters of the book (Chapters 11and 12)show the op-

    eration and maintenance of a cathodic protection system, and how to

    evaluate

    the

    coatings system

    in

    place.

    The

    Appendixes containmaterial

    basic

    to the

    knowledge

    of all

    corrosion engineers.

    Atthe end ofthis

    book,

    the

    reader

    w i ll

    bewellon the way tobeinga

    capable corrosion engineer.

    Edward

    G.

    Peattie

    Professorof

    Petroleum Engineering

    Mississippi State University

    vlii

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    P r e f a c e

    t o F i r s t E d i t i o n

    Howdo

    people become pipe line corrosion engineers?

    N ot by

    obtain-

    ing a degree in the subject, for no such degree is offered. Many corro-

    sion engineers hold degreesin chemistry, chemical engineering, elec-

    trical

    engin eering, or any one of several others. M an y others either have

    no

    degree, orhave studied in some field apparently or actually remote

    fromcorrosion. All of these men became corrosion engineers by on-the-

    job

    experience

    and by

    individual

    studysom eby trial-and-error

    meth-

    ods, having been assigned

    the

    responsibility

    of

    protecting

    some

    struc-

    turefrom

    corrosion; some by workingwith people already experienced.

    That this should be the case is not surprising, particularly when the

    protection of un dergro und stru cture s against corrosive attack is still as

    much

    an art as it is ascience. Say, rather, tha tit is atechnology; mosto f

    the design procedures used areeither em pirical, or, atbest, arebasedon

    empirically

    modified theory. Almost every cathodic protection system

    installedhas to be adju sted , by tria l, to do its job properly. It is com m on

    experience thatno twojobs are alike; every new project contains some

    surprises, some conditions

    not

    previously encountered.

    These things are true for two main reasons. First, we do not as yet

    knowenough aboutth e subject; there is

    still

    room for the development

    of more powerful an alytic al m ethods. Second, the soil is a bewilder-

    inglycomplex environ m ent,

    an d

    structures placed thereinaffect

    one an-

    other in

    very complicated ways. Almost never

    can we

    m easure directly

    a

    single qu antity wh ich

    weseek;

    what

    our

    meters usually indicate

    is the

    ix

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    result of w hat we are looking for and a n um ber of par t ia l ly un kn o w n

    disturbing factors.

    Thecorrosion

    engineer, then, must

    be to a

    large extent self-trained.

    And he can

    never expect

    tocomplete

    that t ra in ing . This m anual

    is an

    attempt

    to

    present

    some

    workable methods

    of

    doing some

    of the

    th ings

    th e pipe line corrosion engineer is called upon to do. In no case is the

    method given necessarily th e method; it is merely one method. If, by

    use of

    this

    manual,some

    corrosion

    engineers

    avoid

    someof the

    pitfalls

    intowhichIhave fa l len ,andsave tim eand

    effort

    inobtaininga ndinter-

    preting field data, then I w ill be happy tha t m y tim e has been w ell spent

    setting down some

    of the

    experiencea

    smal l par t

    of

    which

    has

    been

    his own,

    a

    very large share

    of

    w hich

    is that of

    m a n y

    othersand

    thus

    providing,

    in a

    way,

    a

    shoulder

    to

    look over.

    Marshall

    E.

    Parker

    Houston, Texas

    January

    18,

    1954

    x

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    1

    S o i l R e s is t iv i ty S u r v e y s

    Pipe linesmay be cathodically protected ineither earthor water.To

    determine if cathodic protection may be used to prevent corrosion of

    steel pipe lines,

    we

    must first learn

    how to

    measure

    the

    resistivity

    of

    these en vironm ents .

    SoilResistivity Units

    Theuni tofsoilresistivity is the

    oh m-centimeter,

    usually abbreviated

    ohm-cm;the resistivity of a given soil is nu m erically equal to the resis-

    tance

    of a

    cube

    of the

    soil

    one

    centimeter

    in

    dim ensions,

    as

    measured

    from opposite faces (Figure

    1-1).

    The resistance of a rectangular solid

    other

    than

    a

    cube

    is

    given

    by

    whereW , L, and D are the dim ension s in centimeters, as show n in Fig-

    ure

    1-1,and p is the resistivity; the un it m ust be ohm -cm inorderfor the

    equation

    to be consistent. The resistance between any two terminals, of

    any

    size

    and

    shape,

    in

    contact with

    a

    body

    of

    soil,

    of any

    extent ,

    is de-

    termined

    by the size and spacing relationships and by the resistivity of

    th esoil.

    For

    simp le cases,

    th e

    resistance

    can be

    computed,

    but the

    math-

    ematical complexities

    are

    often very great.

    1

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    Figure

    1-1.(a)Resistivity @ )in ohm-cm isnumerically

    equal

    to the re-

    sistance R)inohmsbetweenopposite facesof acubeone cm on the

    side,(b)

    Resistance

    of arectangularsolid,(c)Soilbox,inwhich is ob-

    tained

    bymeasuringthe resistance

    between

    theplanesof the two po-

    tential

    pins.

    Two-Terminal

    Resistivity

    Determination

    An

    apparatus similar

    to

    that illustrated

    in

    Figure

    1-1 may be

    used

    to

    determine

    th e

    resistivity

    of

    soil samples;

    in

    corrosion investigations,

    however, it is much more

    useful

    to measureth e soil in place.

    If

    tw o

    term inals

    are

    placed

    in the

    soil,then

    itwillbe

    possible

    to

    deter-

    mine its

    resistivity

    by

    measuring

    the

    resistance between

    the two

    elec-

    trodes.If

    they

    are

    placed close together,

    it

    w ill

    be

    necessary

    to

    m aintain

    aknown

    and

    fixed distance between them ;

    if

    they

    are far

    enough apart ,

    surprisingly

    enough ,

    the

    indicated value

    isvirtually

    independent

    of the

    distance. Either AC or DC may be used, and the resistance may be de-

    2

    Pipeline Corrosion

    and Cathodic

    Protection

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    Soil Resistivity Surveys 3

    Figure 1-2.

    Shepard canes

    for

    soil resistivity measurement. Current

    from

    a

    three-volt battery (two flashlight cells)

    is

    passed through

    the

    soil

    between two

    iron electrodes mounted

    on

    insulatingrods. Current flow

    is

    measuredby adouble range milliammeter (0-25 and0-100)graduated

    to

    read directly

    in

    ohm-cm

    (10,000-400and500-100).

    Cathode

    is

    made

    largertoavoid

    polarization;

    accuracyisabout 6o when tipsaresepa-

    rated

    by 8inchesormore. Meter,

    batteries,

    andswitcharemountedon

    anode

    rod.

    termined

    by

    measuring current

    and

    potential,

    or by a

    bridge

    circuit,in

    whichthe unknown resistance is compared to one which is within the

    instrument.

    Figure 1-2illustrates Shepard canes, which use DC impressed be-

    tween

    two

    ironelectrodes.This apparatus

    is

    rapid

    in

    use,

    but

    gives

    the

    valuecorresponding to a small sample of soil, in the immediate neigh-

    borhood

    of the

    electrodes. Figure

    1-3

    shows

    an AC

    bridge-type appa-

    ratus; this

    deviceis

    alsovery rapid

    in

    use,

    but it,

    too, measures only

    a

    smallsample. Numerous variations of the latter are on the market.

    Four-Terminal

    Resistivity

    Determination

    To include a larger sample of the soil and measure the resistivity at

    greater depths, the four-terminal or Wenner method may be used. The

    basic circuit is shown in Figure

    1-4;

    the following figures (Figures 1-5,

    1-6, and 1-7) show some of the specific methods based on this tech-

    nique. Detailsofoperationvary withtheparticular instrument

    used,

    but

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    4 Pipeline Corrosion

    and

    Cathodic Protection

    Figure 1 3.

    AC soil rod. Current from an AC source (usually a battery,

    buzzer,and

    condenser)

    is

    passed through

    the

    soil between

    a

    steel

    rod

    andan

    insulated

    steel tip.Theslidewire isthen adjusteduntilno

    signal

    is

    heard

    in the

    headphones;

    at thepointof

    balance

    Inpractice,theslidewire R

    R

    B

    isgraduated to readRdirectly; then

    = R - C, whereC is aconstantfor theparticular rod, determinedby

    calibrationin a solution of known resistivity.

    Figure 1 4.Four-terminal Wenner)measurementofsoil resistivity. Dis-

    tance (b), depth of electrode, must be small compared to (a). The basic

    formula is

    Theresistivity

    is averaged to a

    depth approximately equal

    to the

    elec-

    trode spacing (a).

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    So/7Re sist ivity Surveys

    5

    Figure 1 5. Ammeter-voltmeter measurement of resistivity.Astorage

    battery of drycellsmay be used forcurrent. Coppersulfateelectrodes

    will

    help avoid

    polarizationerrors.The voltmeter used must behighre-

    sistance, or a potentiometer may be

    employed.

    If the

    distance

    (a) is

    made

    5 feet,

    2

    A >

    inches,thenthe

    formula

    simplifiesto

    Directionof current

    should

    be reversed, andreadingsaveraged, to bal-

    ance

    out

    extraneouscurrents

    or

    potentials

    in the

    soil.

    the principle is common to all. It should be noted that the resistance

    measured

    is

    that between

    the two

    inner

    or

    po tentia l electrodes;

    the

    outer pair serve

    to

    introduce

    the

    current into

    the

    soil.

    The value obtained is an

    average

    value to a depth approximately

    equal

    to theelectrode

    spacing; actually

    it is

    influenced

    to

    some degree

    by

    soil lyin g at even greater depths. There is no sharp divid ing line but

    the

    influence

    ofsoil at

    greater

    and

    greater depths becomes smaller

    and

    smaller.

    Other

    Methods

    There are at least three possible indirect methods of measuring soil

    resistivity in which no contact is made with the soil at all. An induction-

    type

    pipe locater gives an indication of the resistivity below it and may

    be calibrated to yield fairly acc urate resu lts. In general this method

    may

    bevery

    useful

    inscoutingout low -resistivity areas w hich canthen

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    6 Pipeline Corrosion

    and

    Cathodic Protection

    Figure

    1-6. Vibroground

    (simplified

    diagram).Vibrators

    V ,and

    V

    2

    are

    synchronized;

    Vi

    converts the

    battery's

    DC

    into

    AC; the

    slidewire

    S is

    adjusteduntiltheIRdrop

    across

    R,justbucks out the current in the po-

    tential

    circuit,

    asindicatedby azerodeflection on the

    galvanometer

    G;

    R

    is

    then

    readdirectly on the

    slidewire,

    and isobtained

    from

    =

    2xaR

    be explored more precisely by one of the methods already described.

    The v alue and phase angle of the impedance (high-frequ ency) be-

    tween

    tw o

    parallel conductors lying

    on or

    parallel

    to the

    surface

    is a

    function of thesoil resistivity, and thu s a device could be b ui lt w hich

    would

    employ this principle. It is also true thatthe tiltof theradiation

    field of a remote radio transmitterat the surface of the earth is a func-

    tion

    of the

    soil resistivity. Both

    of

    these methods offer some promise

    of

    development into very rapid and possibly automatic systems for the re-

    cording of resistivity, but the development has not yet been done.

    Locating Hot Spots on BareLines

    Bare lines, particularly gathering lines, are often so situated that the

    point of

    m ax im um economic return

    for cathodic

    protection

    is not the

    preventionof all leaks, but the preven tion of85-95%of them . This can

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    Soil Resistivity Surveys

    7

    often be done at acost as low as 15% of that of full protection by the

    application

    of

    galvanic

    anodesusual ly

    magnesiumto

    the hot

    spots''

    or

    areas

    o f

    m ax im um corrosiveness. This

    has

    been shown

    to

    cor-

    relate highly with resistivity so that a system of locating areas of

    low,

    and

    of

    relatively

    low,

    resistivity,

    is the

    indicated technique. Such

    apro-

    cedure is known as a soil resistivity survey, and consists of a series of

    mea suremen ts taken along the line (or right-of-w ay for a planned lin e),

    using any of the methods described. The four-point method is most

    commonly used.

    Readings should

    be

    ta ken according

    to a

    systematic procedure; there

    is

    some conflicthere between the demands of science and those of prac-

    ticality. If

    readings

    are

    taken

    atuniform

    spacing,

    th e

    statistical ana lysis

    of the

    entire

    set

    will

    be

    more representative

    of the

    corrosive conditions

    along

    this line,

    as

    compared

    to

    other lines.

    In

    other w ords, such

    a

    proce-

    dure w ill give

    th e

    m a x i m u m

    of

    general information.

    The

    m a x i m u m

    of

    useful

    inform ation, however useful

    in the

    design

    of a hot

    spot protective

    Figure 1-7. Soil resistivity Megger (simplified diagram).

    DC

    from

    the

    hand-cranked generator

    G

    isconvertedto AC by thecommutatorC

    c

    ,

    and enters thesoilthroughC

    1

    and C

    2

    , after passing through the current

    coil;

    the AC potential picked up between

    P

    1

    and

    P

    2

    is converted to DC by

    commutatorC

    p

    and is fed to the potential

    coil.

    The needle comes to rest,

    under the opposing forces from the twocoils,at a point which indicates

    the

    resistanceR.

    is

    then obtained from

    =

    2iraR

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    8

    Pipeline Corrosion

    and

    Cathod ic Protection

    system,

    is notobtained in

    this way,

    butratherby

    some such method

    as

    th e

    following:

    1. A

    reading

    to be

    taken

    at

    least every

    400

    feet.

    2. A reading to be taken w herever there is a visible chan ge in soil

    characteristics.

    3. Two successive readings should not

    differ

    by aratio greater tha n

    2:1

    (when

    a

    reading

    differs

    from

    th e

    preceding

    by

    m ore than this,

    then it is necessary to go back and insert a rea ding; this should be

    repeated

    unt i l

    condition 3 is met).

    4. As anexceptionto the last

    rule,

    no two

    readings

    need

    be

    taken

    closer than

    25

    feet.

    5.

    As another exception to the 2:1 rule, it does not apply when the

    lower

    o f the two

    readings

    is

    greater tha n

    20,000

    ohm-cm.

    The

    fig-

    ures given in this set of criteria may be varied for-specific cases;

    theforegoingset hasbeen

    found

    useful andeconom icalin thesur-

    vey of over a mill ion

    feet

    of gathering lines.

    For

    this type

    o f

    survey, readings w ould

    be

    taken w hic h correspond

    to

    th e

    soil at pipe depth. This means that holes will have to be drilled or

    punched

    for thesingle-rod

    apparatus.

    The

    four-terminal

    system

    should

    be used witha spacing of about 1

    '/2

    times pipe depth; very often a 5-

    foot, 2'/2-inch

    spacing (which makes the multiplier

    2ira

    just equal to

    1000) is well suited for this purpose.

    Data obtained

    in the

    survey

    are

    plotted

    on a

    diagram representing

    th e

    length of the line, as illustrated in Figure 1-8. The vertical resistivity

    scale

    is

    logarithmic, since resistivity ratios

    are of

    interest, rather

    than

    their

    differences. From such

    a

    diagram

    the

    hot spots

    can

    readily

    be

    located. This technique

    will

    be

    discussed more

    fully in a

    subsequent

    chapter.

    Surveys forGround Beds

    The resistivityof the soil in which a ground bed is to be installedis

    one of the primary design quantities involved. It is most importantto

    get as low a total resistance as possible in order to obtain the necessary

    current

    output with

    the

    m i n i m u m a m o u n t

    o f

    power. Unlike

    the

    survey

    to

    determine

    corrosiveness,

    as in the

    preceding topic,

    in

    this case

    th e

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    Figure 1-8. Soil resistivity profile. Measurements taken

    by any of the

    methods described

    are

    plotted

    as

    ordinates(using

    alogarithmicscale),

    with distances along

    the

    pipeline

    as

    abscissas.

    resistivity

    to

    great depth

    is

    imp or t an t.

    For

    this reason,

    the

    four - te rm inal

    method is the only one

    useful

    here. It is customary to take readings at

    5-,

    10-,and

    20-foot

    pin

    spacing (actual values used

    are 5

    feet,

    2

    l

    /2

    inches;

    10 fee t , 5 inches; and 20 fee t , 10 inches ; g iv ing mul t ip l ie r s of

    1000,

    2000,

    and4000, respectively).

    The prospective site should be marked off in a rectangular grid, with

    spacings

    of 50 or 100

    feet,

    and

    readings taken

    at

    each grid intersection;

    where differences

    are too

    great, intermediate readings should

    be

    taken.

    Soil Resistivity Surveys 9

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    10 Pipeline Corrosion

    and

    Cathodic Protection

    These

    diagrams should alw ays be plotted in the

    field

    so that a comp lete

    picture

    will

    be

    obtained. Contours

    can be

    drawn,

    as

    indicated

    in

    Fig-

    ure

    1-9.

    If

    colors

    are used, the readings at all three pin spacings can be

    put

    on the same diagram; only one is shown

    here.

    Note that the values

    chosen for contours are logarithmic, as were the vertical scales in the

    line resistivity survey.

    Area Surveys

    Where a set ofpiping and other underground structures is spread out

    over an area, as in a refinery or chemical plant, a survey similar to the

    one

    jus t described w ill

    furnish

    information

    useful

    both

    in the

    prediction

    ofcorrosiveness

    and in the design of protective systems. The spacing

    used between readings

    is

    u sua lly greater

    than for

    ground

    bed

    design.

    A

    Figure 1-9.

    Resistivity

    plat.

    Resistivity readings taken

    at

    spaced inter-

    vals, with

    additional

    readings

    at

    criticalpoints,

    are

    indicated

    by the

    small

    figures.

    The

    curves represent

    linesof

    equal resistivity. Such plats

    are of

    value

    in

    locating sites

    for

    groundbeds

    and in

    their design.

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    SoilResistivity Surveys

    11

    Figure 1 10.

    Resistivity

    histogram. Equally spaced resistivity readings

    taken

    over

    an

    area

    or

    along

    a

    pipelineroute

    are

    plotted according

    to the

    frequency ofoccurrenceofreadingsin thedifferent ranges. Note that

    successive

    ranges cover equal resistivity ratios, rather than arithmetic

    differences.

    pre l iminary

    spacing

    of 400

    feet

    is

    often used, with intermediate posi-

    tions used where necessary

    to get a

    clear picture.

    As in the

    ground

    bed

    survey,

    readings

    are

    usually displayed

    on a

    resistivity contour

    map of

    th e

    plant site. Usually only one pin spacing isused, and the most fre-

    quent

    value is the nominal five-foot spacing already mentioned.

    In

    addition to thegeographical distribution shown on the resistivity

    plat, it is useful to

    prepare

    a

    histogram,

    or

    frequency distribution,

    as

    indicated in

    Figure 1-10. This shows

    the

    number

    of

    readings found

    in

    various classes or

    ranges

    of

    resistivity; these ranges should

    beloga-

    r i thmic,as are the

    contour intervals

    on the

    plat already described.

    Logarithmic

    Resistivity Ranges

    Three examples have already been given

    of

    logarithmic treatment

    of

    resistivities. There

    is

    sound scientific basis

    for

    this approach, aside

    from

    the

    intuitive observation that ratios

    are

    more important than differ-

    ences. It hasbeen found that large numbersofresistivity readings, when

    expressed

    as

    logarithms, tend

    to fall

    into

    standard

    distributions.

    The

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    12 Pipeline Corrosion and Cathodic Protection

    standard distribution is a well-known and extremely useful concept in

    statistical analysis.

    A consequence of this is that two extensive structures (such as pipe

    lines) each exposed

    to a

    wide variety

    of

    soils

    can be

    compared

    as to

    their

    corrosion exposure most accurately

    by

    comparing their

    logarithmic

    mean

    resistivities.The logarithm ic mea n resistivity of a set of resistivi-

    ties is the value whose logarithm is the average of all the logarithms of

    the measured values. These can most easily be averaged by grouping

    them into

    classes,

    as shown in Figure 1-11,where the logarithmic m ean

    of 115

    different

    readings is

    found

    to be

    14,900

    ohm-cm.

    It is almost universal practice to

    choose

    a ratio of

    2:1

    for the succes-

    sive values used in any loga rithm ic system, for contours, h istog ram s, or

    the calculation of a me an. Three

    different

    systems are in widespead use:

    thetw o

    already illustrated

    (A)

    based

    on 100

    ohm-cm,

    as

    used

    in

    Figures

    1-9 and

    1-10;

    (B ) based on

    1000 ohm-cm,

    as

    used

    in

    F igure

    1-11;

    and (C)

    which

    is not

    truly logarithmic,

    in

    that

    th e

    ratio

    is not al-

    ways the same. All three are shown here for comparison:

    A) B) C)

    50

    62.5

    50

    100 125 100

    200 250 200

    400 500 500

    800

    1,000

    1,000

    1,600

    2,000 2,000

    3,200 4,000 5,000

    6,400 8,000 10,000

    Scale

    (C) has the

    advantage

    in

    that

    all of the

    values

    are

    round

    num bers whereas

    if

    either

    (A) or (B) is

    extended

    fa r

    enough

    in

    either

    direction, the numbers tend to become awkward. On the other hand,

    when a

    mathematical analysis

    is

    made

    of the

    data,

    the

    irregular ratios

    involved in scale (C) introduce complications. Note,

    when

    (C) is used

    for

    a

    histogram,

    the

    horizontal widths

    of the

    cells should

    be

    made

    proportional

    to the

    logarithms

    of the

    ratios.

    Log 2 =

    0.301,

    log 2.5 =

    0.398;

    so the

    ratio

    of the two spaces

    should

    be

    about 3:4.

    The corrosion technician now has vario us methods at his disposal to

    measure the resistivity of the soil in which the pipe line is to be in-

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    Soil Resistivity Surveys

    13

    Figure

    1-11.Summary

    of

    soilresistivity measurements.

    stalled. The question may now be asked: What if the pipe line is to be

    installed

    in

    waterwould

    the

    same methods

    of

    measurement work?

    The answer is

    yes,

    but w ith reservations. Ac tually, a single sam ple of

    the water

    is

    enough ,

    and it can be

    measured

    in a

    soilbox,

    as

    shown

    in

    Figure 1-12. The countless va riations of resistivity w hich w e have

    shown in

    Figure

    1-9 for

    soil

    do not

    exist

    in the

    water environment ,

    and

    so onere sistivity valu einohm -centimetersisusual ly enoughfor the en-

    gineer

    touse. For soils, as we have seen, it is more complicated.

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    14 Pipeline Corrosion and Cathodic

    Protection

    Figure 1-12.Typical connections

    for use of

    soil

    box

    with varioustypes

    ofinstruments. (Courtesy

    of M. C.

    Miller Co., Inc.)

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    So/7 Resistivity Surveys

    15

    Summary

    The

    resistivity

    of

    soil

    is

    usually

    measured

    by the

    four-pin

    method

    with

    theVibroground(Figure

    1-6),

    possibly

    the

    easiest

    instrument

    to

    use.It is

    possible

    to

    attach

    a set of

    pins

    andleads

    which will minimize

    th e

    tim e to get soil resistivities, and a com plete surve y may be done in a

    relativelyshort tim e. The new est examp le of the soil resistance m eter is

    shown in

    Figure 1-13

    and has

    been available since

    1981.

    Its

    advantage

    is

    that there

    are no

    moving parts

    and no

    vibrators

    to

    change. Although

    called a

    four-pin

    soil resistance meter,

    it is

    also excellent

    for

    m easuring

    water samples

    in a

    soilbox.

    Figure1-13.Four-pinsoilresistance meter.

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    2

    Potential

    S u r v e y s

    Pipe-to-Soil

    Potentials:Electrodes

    The potential difference between aburied pipeand thesoilis ofcon-

    siderable importance, either ininvestigatingth e corrosive conditionsor

    in

    evaluatingtheextentofcathodic protection being applied. This qu an -

    tity actuallyis measured by connectingan instrumen t betweenthepipe

    itself

    (direct metallic contact)

    and a

    special electrode placed

    in

    contact

    with the soil. Thiselectrode is also called a half cell .

    The most common typeof electrode in use is that which employs a

    m etal-to-electrolyte ju n ctio n consistingofcopper incontact

    with

    asatu-

    rated solutionofcopper sulfate; this particular com binationis madeof

    easily

    available m aterials and is very stable. Figure 2-1 shows two typi-

    cal electrodes. Other types in use

    are:

    1. The hydrogen electrode, used

    only

    in laboratory investigations.

    2. The calomel electrode, used often in fresh water or saltwater.

    3. The

    lead/lead

    chloride electrode, frequently employed in studyin g

    the corrosion of lead cable.

    4. The silver/silver chloride electrode, used in seaw ater because it is

    not subject tocontam inationby salt incursio n.

    5. The pu re zinc electrode (in packaged b ac kfi ll). This is suita ble as

    ape rm an ently installed reference electrode. (Note: all these listed

    electrodes m ust be corrected to give readings sim ilar to thecop-

    per/copper sulfate

    halfcell.

    See Appendix C.)

    16

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    PotentialSurveys 17

    Figure 2-1. Copper sulfate electrodes. The essential parts are: 1) a

    piece of copper, to which the instrument is connected; 2) a saturated

    solution

    of

    copper sulfate,

    in

    contact w ith

    the

    copper;

    3) a

    porous mem-

    ber,placed incontact withthesoil.It isessential thatnometal touchthe

    copper sulfate solution

    except

    copper.

    Excess

    c rystals areadded,to en-

    sure

    that the solution always

    will

    be saturated.

    Voltmeters

    One choice for the instrum en t to be used in m easuring

    this

    potential is

    the voltmeter,

    as

    shown

    in

    Figure 2-2; there

    are two

    possible sources

    of

    error

    in its

    use.First,w hi le

    a

    voltm etercorrectly indicates

    the

    potential

    difference across it sterminals,

    the current which flows through the in-

    s t rument (a voltmeter is essentially a

    mi l l iammeter )

    introduces an IR

    drop in the rest of the circuit, which is not included in the reading. For

    example,

    if the

    resistance

    of the

    external circuit (pipe, lead wires, soil,

    and

    electrode)

    is

    one-fourth

    the

    resistance

    of themeter,

    then

    the

    meter

    wil l

    read only four-fifths

    of the

    total potential;

    the

    error

    wil l

    be

    20%.

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    18 Pipeline Corrosion and Cathodic Protection

    Figure 2-2.

    Voltmeter measurement ofpipe-to-soil

    potential.

    Connec-

    tionto the

    pipe

    may be by

    means

    of aweldedor

    soldered leadwire

    as

    illustrated),by a contact

    bar,

    or bymechanical

    connection

    to a

    valve

    or

    fitting

    above the surface. Thelatter

    should

    be used withcaution,as

    flangedfittings

    sometimes

    introduceextraneouspotentials.If thesoilis

    dry,a

    little

    watermay beaddedtolowerthe contact resistance; it isusu-

    ally

    adequate

    to dig a

    littlebelow

    the surface.

    A second source

    of

    error

    is

    that

    the

    passage

    of

    current through

    the

    circuitmay polarize the electrode or even the pipeitself, and so change

    the potential we are trying to measure. Both of these errors may be

    minimized by the use of a high-resistance voltmeter; not less than

    50,000ohms per volt is recomm ended, and this is often too low. Read-

    ings

    should always be taken on two

    different

    scales (introducin g two

    different values of meter resistance); if they are in substantial agree-

    ment ,

    th e

    value

    may be

    accepted.

    In

    th enex t section, methods w illbegivenforobtainingthecorrected

    value when

    the

    error

    due to

    voltmeter resistance

    is not too

    high (see

    Equations 3-2 and 3-3).

    There

    is

    also available

    a

    special dual sen sitivity voltm eter w hich

    offers

    two diffe ren t resistance va lues on the same

    scale.

    If the reading is

    the same for these two (the change is m ade by m erely p ush ing a button),

    then no correction is needed. If pushing the button makes a small

    change in the reading , then a very simp le correction can be m ade. An d,

    finally,

    if the change is large, an equation com parable to those cited pre-

    viously can be used. This meter isvery useful for m akin g rapid poten-

    tial

    readings.

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    Potential Surveys

    19

    Figure 2-3.

    Slide-wire

    potentiometer, a)

    Basiccircuit.When

    the

    slide-

    wire S is adjusted so that the galvanometer G shows no deflection, then

    the unknown potential connected

    to the

    terminals

    can be

    read directly

    on

    the slide-wire

    scale.

    This simple

    circuit

    could be used only if the bat-

    tery

    voltage w ere

    constant,

    b) Modified

    circuit,

    with provision for adjust-

    ing

    battery voltage with resistor

    R

    B

    ,

    using standard

    cellSC for

    calibra-

    tion.

    ResistorR

    0

    protects the galvanometer against excess currents; it

    isshorted out by the switch when the instrument is almost perfectly bal-

    anced. Mostinstrumentsfor

    corrosion

    usehavetwo ormorescales,in-

    stead of the one shown here.

    Slide-Wire

    Potentiometer

    These problem s largely

    are

    overcom e

    by the use of the

    potentiometer,

    an instrum ent which draws no current from th e circuit at the pointof

    balance.

    Itshouldberemem bered,

    however,

    thatcurrentisd rawn while

    balancing is in progress and

    that

    some polarization m ay occur. Figure

    2-3 shows this instrument and indicatesitsuse.

    Potentiometer-Voltmeter

    Another

    approach

    to the

    problem

    is the potentiometer-voltmeter, one

    form

    of

    which

    is

    shown

    in

    Figure 2-4. Both

    of

    theseusefulinstrum ents

    suffer

    a

    disadvantage w henfluctuating potentials

    a re

    encountered,

    as in

    a stray-curren t area, since it is impossible to follow rapid fluctuations

    with them.

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    20 Pipeline Corrosion and

    Cathodic Protection

    Figure 2-4. The potentiometer-voltmeter, a) Shows the basic circuit.

    When the galvanometer deflection iszero,the external potential con-

    nected to the terminals is the same as that portion of the battery voltage

    which is indicated onvoltmeter V ;

    this,

    then, is adirect reading of the

    unknownpotential.In (b)several refinements have been added:(1)w ith

    switch

    $

    open,ahighrangeisadded; 2) the tworesistorsR ,andR

    2

    ,of

    different values, provide a fine and coarse adjustment, and 3) switch S

    2

    controlsaprotective resistor, similar tothatinF igure 2-3. More thantwo

    ranges are possible, and it is also possible to use the same instrument

    asanammeterby

    building

    inshunts.

    Vacuum-Tube Voltmeter

    This instrument (not illustrated) has, through

    the use of

    transistors

    and

    other recent developments, now reached a stage of reliabilityand

    stability

    w hich makes

    it

    quite

    useful in the

    field. Battery-poweredunits

    are

    availablewith input im pedances

    as

    high

    as 10

    m egohms,

    so the

    cir-

    cuit

    resistance e rror ceases to be a problem . They po ssess an ad ditiona l

    advantage

    over

    th e

    various poten tiom eter types

    of

    ins truments

    in

    that

    theydo not

    have

    to be

    balanced,

    and

    hence

    may be

    used

    to

    follow

    fluc-

    tuating potentials w ithout

    difficulty.

    Solid-State

    Voltmeter

    This

    instrument

    (Figure 2-5)

    is the

    successor

    to thevacuum-tube

    volt-

    meter

    and

    differs

    onlyin the substitutionofsolid-state transistorsfor the

    more

    vulnerable

    vacuum

    tubes.

    T he

    resistance problems have been vir-

    tual lye l imina ted ,and accurateresults m ay beobtainedby

    no ntechnical

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    Potential Surveys 21

    personnel .

    A

    p ar t icu lar model

    has

    selectable

    inpu t

    resistances

    of

    1,

    10,

    25, 50,

    100,

    and 200

    megohms. This al lows

    theuserto

    determine pipe-

    to-soil

    potent ia lsin such

    diff icul t

    env i ronmen tsasci ty pavem ents . The

    range in reading varies from0.1 m v to 20 m v. This is a rugged ins tru -

    ment

    for the

    technic ian

    who has to

    take many readings .

    Figure 2-5.

    Solid-state DC voltmeter. Courtesy of M. C.

    MillerCo.,

    Inc.)

    MulticombinationMeter

    This

    is the

    ins trument most often used

    by

    corrosion

    engineers

    be-

    cause

    of its

    versatility.

    It is a

    developm ent

    of the

    potentiometer-voltme-

    ter

    already described

    but has the

    following particular characteristics,

    as

    shown

    by the

    latest 1983 model

    in

    Figure 2-6.

    The

    right meter

    has a

    l iquid crystal display with5 ranges from - 20 mv to 200 v andw i th

    selectable i n pu t resistances

    of

    1-200 m ego hm s.

    The

    left meter also

    has

    a liquid

    c rystal display

    an d

    serves both

    as a

    vol tmeter

    and an

    ammeter .

    The

    four vol tage ranges include- 20 mv to 20 v, and theamm eter range

    is from

    20

    ma to 20 a. As an ohmmete r , it reads from

    2 0

    o h m s to

    2000 ohms . Th i s ins t rumen t

    is

    sti l l ava i l ab le w i th

    the

    convent ional

    m o v i n g

    pointer dials , which are not as easy to read as are the l iquid

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    Potential Surveys 23

    Figure

    2-7. Theelectronic potential

    meter.

    (Courtesy of M. C.

    Miller

    Co.,

    Inc.)

    whe n

    the

    electrode

    is

    placed directly over

    the

    pipe.

    The only way in

    whichthe

    theoretically

    correct

    reading could

    be

    taken would

    be toplace

    th eelectrode

    adjacent

    to thepipe,or to use a complicated nullcircuit

    involving

    two or more

    electrodes,

    in

    which

    the

    effect

    of the IRdrop is

    canceled out. Both of these are quite t ime-consuming, and thus have

    gained little favor.

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    24 Pipeline Corrosion and Cathodic

    Protection

    Figure 2 8. Potential meter with optional accessory electrode exten-

    sion.

    Courtesy

    of M. C.

    Miller

    Co., Inc.)

    Pipe Line

    Connection

    As

    shown in

    Figure

    2-2,

    connection

    to the

    pipe

    mustbe

    made

    by an

    insulated lead wire

    or by an

    insulated contact

    bar or,

    best,

    by

    permanent

    test stations installed along

    the

    pipe line

    at

    regular intervals.

    The

    advantage of the

    test

    station is that, once it is installed, itwillnot be

    necessaryto damage the

    pipeline

    coating to

    make

    contact

    with

    the

    line.

    Figure2-10shows a typical installation. It can be

    seen

    that

    aportionof

    the

    coating

    isscraped off ,and thewireisthen attachedto thelineby a

    process known

    as cadwelding.

    This

    is a

    small thermite unit using

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    Potential Surveys

    25

    Figure 2-9. Current

    and

    potential field around

    a

    pipe.

    The

    dotted

    lines

    represent

    the

    flow

    of

    current

    to or

    from

    a

    pipe lying

    in

    soil

    of

    uniform

    resistivity; thedashed

    lines

    represent equal differences ofpotential. It

    can

    be seen that no

    point

    on the surface is at the samepotentialas that

    immediately adjacent

    to the

    pipe,

    but an

    electrodeplaced

    at A

    repre-

    sentsa closer approximation thanoneplacedat B.

    a l umi num

    powder to produce enough heat to bond the copper wire to

    th e

    steel. Then

    the

    connection

    and the

    surrou ndin g bare metal

    are

    coated

    with a

    coating similar

    to the

    pipe line coating

    and

    usually f in-

    ished with tape. The lead wire isthen brou ghtto thesurfaceand isusu-

    ally

    raised to a heightof

    five

    feet, where a box containinga lead will

    make connection of the testing meter very convenient. When the test

    station isinstalled, it isusually convenient to use it as one end of a test

    section for

    m easuring l ine current ,

    as

    shown

    in the

    next chapter.

    SurfacePotentialSurveyfor Corrosion

    Figure 2-11 represents the current and potential fields around a sec-

    tionof p ipe line w ith a single active corroding (ano dic) area. Th e distri-

    bution ofpotential along th e surfaceof theearth above th epipe clearly

    indicates th e locationof theactive area;thus asurveyo fsurface poten-

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    26 Pipeline Corrosion and Cathodic Protection

    Figure

    2-11.Potential field surroundingasingle anodic point.Aniso-

    latedanodic pointon aburied pipe linecan bedetected easilybysur-

    facepotentialmeasurements,provided that readings

    are

    taken

    at

    suffi-

    cientlyclose spacing.

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    Potential Surveys 2 7

    tials

    along

    th e

    length

    of a

    pipe lin e should

    be of

    value

    in

    locating

    corro-

    sion. Figure 2-12 diagrams th e procedure for making such a survey,

    while

    Figure

    2-13

    shows a typical pipe-to-soil potential of a protected

    line.

    Variations in

    soil resistivity introduce potential differences which

    m ay

    mask those sought, so the problem is by no means as simple as it

    might

    appear. Another

    drawback to

    this

    methodand a

    very serious

    oneis

    that

    i twil lnot

    disclose

    a

    hig hly localized

    cell,

    where

    the

    anode

    andcathodeare

    very

    close

    together,as for

    exam ple,

    the

    common con-

    centrat ion cell where

    th e

    anode

    is on the

    bottom

    of the

    pipe

    and the

    cathode

    on top, at the same location.

    Pipe-to-Soil Potential

    as a

    Criterion

    of

    Cathodic Protection

    It

    is almo st un iver sally accepted that a steel structure unde r cathodic

    protection isfully protected if thepotentialis atleast0.85-voltneg ative,

    referred

    to a

    standard copper-saturated copper

    sulfate

    electrode placed

    in

    th e electrolyte immediately adjacent to the metal surface. The entire

    structure is

    fully

    protected,

    of

    course,

    onlyif this criterion is met at

    ev-

    erypoint on the surface. This is not a m inimu m requirement ; it is a

    m a x i m u m .

    In

    other words,

    it is

    almost certainly true that protection

    is

    complete when this is achieved. It is also possible to have complete

    freedom from

    active

    corrosion

    at lower potentials.

    As m en tion ed, it is imp racticably slow to place the electrode imm edi-

    ately adjacent

    to the

    pipe surface;

    it is

    completely impossible

    to

    take

    a

    reading at every point of the surface. As a consequence of these two

    difficulties, it is generally accepted that th eelectrode is to be placed in

    the

    soil im m ediately over

    th e

    l ine;

    it is not

    difficult

    to

    show that,

    for a

    well-coated line, this is as good as nex t to the pipe. F or a bare lin e, this

    is not

    t rue ,

    but

    bare lines

    are

    rarely

    fully

    protected

    in any

    event.

    The

    other

    difficulty

    isavoided byassumingace rtain degree ofcontinuityin

    th e

    potential gradient along a line. This assumption is almost always

    valid,

    a nd , itturns ou t , when itbreaks dow n because of discontinuities

    in soil resistivity,

    it

    fails only

    in

    areas which

    are

    virtual ly

    noncorrosive

    without

    protect ion.

    It

    is

    cus tom ary , then ,

    and relat ively

    safe ,

    to

    consider

    a

    coated line

    to

    be

    fully protected

    if a

    survey along

    i ts

    length yields

    a

    reasonably smooth

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    28 Pipeline Corrosion and Cathodic Protection

    Figure 2-12.

    Surface

    potential survey.

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    Potential

    S urveys 29

    Figure 2-13.

    Pipe-to-soil potential of protected

    line.

    Typical distribution

    ofpotential alongaline with cathodic protection unitsat A, B, and C.

    Points

    X and Y are thecritical points; if thepotential remains satisfac-

    toryatthese points,theentire line isprobably adequately protected.

    potent ia l

    curve which does not dip below the value of 0.85 volt; all

    readingsbeing takenare

    wi th

    respect to astandard copper sulfate elec-

    trode.

    Oncea detailedsurvey

    over

    the system hasestablishedthatthelineis

    protected,

    then

    periodic

    checks

    at the critical points

    (low potential

    points betweenunits)canmake itpossibleto know that protection is

    still being afforded. Thissubject

    is

    discussedmore fully later.

    Other

    Applicationsof

    Pipe-to-Soil

    Potentials

    This measurement forms a part of the technique used in several types

    ofstudies, most of which will be described later. Among them may be

    ment ioned:(1)

    interference studies,

    (2)

    stray current

    investigations,(3)

    coatingconductance measurements, and (4) cathodic protection tests.

    Other Criteria

    In

    addition to use of the

    -0.85-volt

    standard for adequacy of a ca-

    thodic protection system, two other methods are in use:

    1.

    Test coupon. Burying corrosion test coupons along

    the

    pipe line.

    These should

    be

    weighed

    and

    connected

    to the

    line

    at

    locations

    possibly

    subject

    to

    extreme corrosion conditions.

    After a

    given

    exposure time, they should

    be

    removed

    and

    reweighed.

    A ny

    loss

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    30 Pipeline CorrosionandCathodic Protection

    in

    weight

    may be

    used

    to

    calculate

    th e

    degree

    of

    protection neces-

    sary.

    2.

    Potentialchange.

    Another

    criterion(called doubtful

    by

    Uh lig*

    but

    oftenused in

    cathodic protection

    design)is to use a

    potential

    change of 0.3 volt when

    current

    is applied as a measure of ca-

    thodic protection. Thisinvolves an interruptedcathodic protec-

    tion

    current measurement, as will be

    shown

    in Chapter 4. Also,

    thisconceptm ay beused in primary designcalculations, as de-

    scribed in

    Chapter

    5.

    Summary

    We have thus seen that, although there are several reference elec-

    trodes (half cells) available for potential difference measurements, only

    the copper/copper sulf ate electrode is used for mo st of the rea ding s the

    corrosion

    engineer will take

    on

    land. Also,

    for

    precision,

    the

    poten-

    tiometer, particularlyin the

    form

    of acombinat ion ins t rum ent ,isprefer-

    able

    to the

    low-resistance voltmeters.

    The

    placement

    of the

    reference

    electrode

    is

    best made

    on the

    surface

    of the

    earth directly

    over the

    bur-

    ied

    pipe

    line.

    Sometimes,th e

    soil

    should bem oistened, although prefer-

    ably

    nothing should

    be

    done

    to

    affect

    th e

    envi ronment .

    For

    contact with

    the

    pipe

    line, it isadvisabletohave test stations installed at regular in -

    tervals along

    all

    major pipe l ines. This will el iminate

    the

    problems

    of

    direct

    metal

    contact

    with

    th e

    pipe

    itself,

    which will

    be

    necessary

    if the

    permanent leads

    are not

    available. Although

    the leap-frog

    system

    maybe

    useful when there

    is a

    distance between test stations,

    it

    would

    be

    advantageous

    to

    have

    a

    reel

    of

    wire available

    to

    extend

    th e

    measure-

    ments along

    the

    pipe l ine , part icularly

    in

    regions near

    th e

    m idpoints

    b e-

    tween rectifiers. Modern methods of pipe-to-soil measurement use re-

    cording vol tmeters, which

    may be

    used

    to

    complete

    a

    series

    of

    pipe-to-soil potentials along

    a

    pipe line

    in a

    very short time.

    * Uhlig ,H. H.,

    Corrosion and Corrosion Control: An

    Introduction

    to

    Corrosion Science

    andEngineering, 2 ndEdition, 1971, John Wiley and Sons, Inc. , New York, p. 225.

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    3

    L i n e C u r r e n t s

    Now that

    w e

    know

    the

    most comm on pipe l ine m easu rem ent, pipe-to-

    soil potential difference, we shall s tudy some other measurements nec-

    essary for corrosion control. The n ex t is l ine curren t m easurem ent.

    MeasurementofLineCurrent in TestSection

    Atest section consists of a len gth of uni nt err up ted pipe l in e (no joints

    other than welds, no f i t t ings) between two points to which an ins tru-

    ment may be connected (see Figure 3-1). The connection points usu ally

    take the form of a pair of permanently attached lead wires; the use of

    contact bars is

    di f f icul t

    and general ly unsat is factory.The resistance of

    the pipe

    itself

    (not the lead wires) between the two points must be

    k n o w n ;

    it

    wi l l usual ly

    be on the

    order

    o f

    0.001 oh m ,

    or may be ex-

    pressed in conductance un i ts , as 1.00 am pe re/m il l ivo l t . To o btain th is

    va lue , the lengthof the section must vary according to thepipe weight ;

    values between 50 and 400 feet are common.

    Voltmeter

    Line

    Current

    Measurement

    The difference in potential between the two leads, mul t ip l ied by the

    conductance of the section,

    wi l l

    give the value of thecur ren t f lowin gin

    the l ine . This difference

    in

    potent ial

    may be

    de termined wi th

    a

    mi l -

    31

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    32

    Pipeline Corrosion

    and

    Cathodic Protection

    Figure3-1.Measurement

    of

    IRdrop

    in

    line section. R

    w

    in

    Equation

    3-1

    istotal resistanceof

    7 ^,

    T

    2

    ,

    L

    1(

    L

    2

    ,

    andL

    3

    ,unlessL

    1

    andL

    2

    are apairof

    "calibrated" leads matched

    to and

    supplied with

    the

    instrument,

    in

    which case

    R

    w

    = T

    t

    + 7

    2

    + ^ -3 only-

    Figure 3-2.Calibration

    of

    test section.

    The

    conductance

    of the

    section,

    in amperes per

    millivolt,

    is given by

    Ifthesetwosectionsare notequal, then

    livoltmeter,

    as

    shown

    in

    Figure

    3-2.For

    currents occurring naturally,

    a

    meter with a full-scale

    deflection

    as low as one millivolt may be re-

    quired; the currents used in cathodic protection give rise to larger

    val-

    ues.

    An

    instrument with

    a

    range such

    as

    this will have

    a low

    internal

    resistance, perhaps as low as one

    ohm;

    the resistance of the lead wires

    will

    thus be of

    considerable

    importance. If the value of the lead wire

    resistance is known, the

    corrected

    reading may be obtained from

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    34

    Pipeline Corrosion and Cathodic Protection

    CalibrationofTestSection

    The conductance of a test section may be approximated

    from

    the for-

    mula

    This

    is

    only

    a

    rough approximation;

    th e

    factor

    m ay

    vary

    from 3.5 to

    as

    high

    as

    5.0,

    and

    further

    variation

    is

    introduced

    by the

    weight toler-

    ance

    for

    lin e pipe.

    By far the

    better method

    is

    that

    o f

    direct calibration ,

    asshown inFigure 3-2. Tw oconn ections areusedforcurrent inp ut ,an d

    tw o

    others (w hich w ill rem ain

    as

    perm ane nt test leads)

    for the

    voltmeter

    connection. Not all of the current

    f lowing

    throughthe ammeter , how-

    ever,

    f lows

    through

    th e

    test section; some

    of it f lows

    through

    a

    remote

    earth path. This effect is quite variable, depending upon coating con-

    ductance and earth resistivity; to correct for it, an additional pair of

    leads is required.

    Stray-CurrentStudies

    W henever fluc tua ting currents or p otentials are observed, stray-cur-

    rent

    effects

    are

    suspected.

    Useful

    clues

    to the

    source

    of

    such strays

    can

    be had

    from

    24-hour recordings of line current potentials. If theactual

    current values are desired, corrections may be made by Equation

    3-1;

    or resistance

    can be

    inserted into

    the

    circuit

    so as to

    makeR

    w

    =

    R

    m

    \

    the

    correction factor

    will

    then

    be

    exa ctly

    2 and may be

    made

    by

    selection

    of

    theproper cha rt, so as to record corrected m illivo lts. Co m pariso n of the

    charts with records

    of

    operation

    of

    suspected equipment

    will often lo -

    cate

    the

    source beyond question.

    Long-Line

    Currents

    A use of

    line current measurement more

    in

    vogue

    in the

    past than

    at

    present is thetracingof long-line currents and the location of the areas

    ofdischarge to earth. If cur ren ts of this type were the

    sole

    cause of pipe

    line corrosion, all of the anodic areas could thus be found ;

    unfor tu-

    nately, however, th e most common attackonbu ried pipes isassociated

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    Line Currents

    35

    with corroding

    cells

    of very small dimensions; very often the anode is

    on the bottom and the cathode on top of the pipe only a few inches

    away;

    line current studies cannot locate such a condition.

    Cathodic Protection

    Tests

    The current flows associated with cathodic protection systems, either

    permanent

    or

    temporary test equipment,

    are

    typically long-line cur-

    rents; a very valu able part of such testing is in the m easurem ent of these

    currents; the application

    wil l

    be discussed in a later chapter.

    Coating Conductance Measurement

    The same thingis true of the determ ination of coatingcondu ctance

    a

    type

    of

    measurement which will grow

    in

    impo rtance

    to the

    corrosion

    engineer in the

    future .

    Line current measurements are muchless sub-

    ject to disturbing factors than are potential measurements and

    offer

    th e

    engineer a valuable approach to this

    difficult

    subject; this

    will

    also be

    discussed later in greater detail.

    Summary

    As

    has already been shown, if test stations along the pipelines have

    been installed, it is very easy to construct a test section for line current

    measurement . Al though the lengths m ay vary for these sections, it is

    advisable to have them at least 100 ft long for 8-inch schedule 40 pipe

    and

    as

    much

    as 400 ft for

    30-inch

    OD

    pipe. Again,

    th e

    multipurpose

    corrosion meter can be used, since values as low as one mill ivolt may

    have

    to be measured. Also, the test section may beused tom easure the

    coating resistance once the conductance of the pipe itself has been cali-

    brated.

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    4

    C u r r e n t

    Requirement

    S u r v e y s

    The

    Problem:Coated

    Lines

    The simplest approach to the

    cathodic

    protection of coated lines is to

    aim at

    obtaining

    a

    pipe-to-soil potential

    of

    0.85 volt

    (to a

    CuSO

    4

    elec-

    trode)

    throughout

    the line.

    Meticulous investigations

    m ay

    show that

    protection can be had at lower figures, but only on bare or very poorly

    coated

    structures

    are the

    savin gs likely

    to be

    great enough

    tojustify th e

    additional engineering work required.

    In

    determining

    th e

    amount

    and

    distribution

    of

    drainage current

    to

    produce

    the

    desired potential,

    tw o

    basic approaches

    are

    possible:

    (1) the

    complete

    protectionof the

    line with tempo rary

    installations,

    these being

    varied and shifted untila satisfactory combination is

    found;

    and (2) the

    determination

    of the

    electrical characteristics

    of the

    l ine,

    and the

    calcu-

    lation of the system from these data.

    The

    first

    method

    is

    almost impossibly complicated

    in

    execution

    and

    is

    seldom even attempted. The second is theoretically possible, al-

    though inpractice a certain amountof trial-and-error procedure isusu-

    ally

    n ecessary. Acompromise techn ique,inwh ichthe trialanderrorof

    testing the

    performance

    of

    various combinations

    is

    done

    on

    paper,

    rather

    than

    in the

    field,

    is

    recommended.

    36

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    Current Requirement Surveys 37

    Principlesof

    Current

    RequirementTest

    Current

    is to be

    drained

    from

    the

    line

    to a

    temporary ground bed,

    and

    th e

    effects determined

    for as

    great

    a

    distance

    as

    they

    are

    m easurable (far

    beyond

    the

    point

    of

    complete

    protection);

    from

    one or

    moresuch

    tests,

    the

    behavior

    of the

    l ine with respect

    to

    cur ren t d ra inage

    can be

    determined with sufficient accuracy

    tocarryout the

    design

    of a

    com-

    plete protective system . The e nd resu lt of this design w ill be the specifi-

    cation

    of

    drainage units

    at

    certain p oints, drain ing specified quan tities

    ofcurrent; the detail design of anode beds to accomplish this is another

    matter.

    Field

    Procedure

    The

    following steps

    are

    taken ,

    in

    order:

    1. Static

    potentials. A pipe-to-soil potential survey is made over the

    entire line; permanent test leads

    are

    recommended,

    but bar

    con-

    tacts may be necessary. Spacing m ay vary from a few hundred

    feet

    on poor coating to several m iles on good coating; often road

    crossings willbe adequate. Readings should be taken at all cas-

    ings

    (reading po tentials

    of

    b oth casing

    and

    pipe),

    and on all

    cross-

    ing lines and other structures w hich m ight either be shorted or be a

    source

    of

    interference

    in

    either direction. Such structures include ,

    in addition to casings, bridges, A-frames, supports of all kinds ,

    and

    sometimes even such things as metal fences and guy wires.

    2. Polarization run. At a chosen location, preferablyone whichap-

    pears

    to be

    suitable

    for a

    rectifier installation,

    a

    temporary dra in-

    agepoint isestablished and a steady current drained for aperiod

    of from

    one to three hours. The pipe-to-soil potential of a nearby

    point

    (within

    a few

    miles ,

    on a

    well-coated line;

    a few

    hundred

    feet on a

    poorly coated one)

    is

    observed du ring this inte rval

    to

    fol-

    lo w

    th e

    course

    of

    polarizat ion.

    The

    va lue

    of

    current

    to be

    used

    should

    be

    large enough

    to

    cover

    a usefully

    long portion

    of the

    l ineperhaps

    all of

    i tbut should

    not be too

    large.

    The

    pipe-to-

    soil

    potential near

    the

    drain

    point should not,

    in

    general, exceed

    three volts.

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    38

    Pipeline Corrosion and

    Cathodic Protection

    3.

    Potential survey.

    An interrupter, either manual or automatic, is

    now

    inserted in the circuit and placed in operation. The schedule

    should consist

    of

    unequal

    on

    and

    off

    periods

    of

    predeter-

    mined duration;

    40

    seconds

    on and 20

    seconds

    off is a

    good

    combination touse.W ith this operating, asurvey should be made

    of

    pipe-to-soil potentials

    at all of the

    points covered

    in 1. Static

    potentials.It is

    im portant that

    the

    same electrode position

    be

    used

    as was used for the static potentia l at each loca tion . At each po in t,

    both the on and off

    potentials should

    be

    read;

    the on

    reading should

    be

    taken just before interruption,

    and the off

    reading as soon as possible after interruption. Care should be

    taken

    that

    these

    two

    readings

    are

    correctly

    identified; the

    length

    of the

    cycle

    is

    used

    fo r

    that purpose.

    It is

    not safe

    to

    assume that

    the

    higher (more negative) readingisalwaysthe

    on

    readingas

    this is not thecasewitha properly insulated lateral orcasing. It is

    recommended that a graph of these values be ma de in the

    field

    as

    th e

    readings are taken in order to detect any peculiarities which

    might call for additional readings. Figure

    4-1

    shows a drawin g of

    an

    automatic interrupter suitable

    for use on the

    above test.

    Figure 4-1.

    Current interrupter. (Courtesy

    of M. C.

    Miller Co., Inc.)

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    Current

    Requirement Surveys

    39

    4. Pola rization and cu rrent

    check.

    The

    series

    of

    po tential readings

    at

    a point near thedrain point, aswell as a

    series

    of current values,

    should be

    continued during

    th e

    potential survey.

    It is

    desirable

    to

    keep

    th e

    current constant throughout

    th e

    test

    if

    this

    can be

    done

    easily. Where this

    is not

    possible,

    it is

    better

    for it to

    change

    smo othly over a considerable range of values than to change often

    and abruptly. If the current change is not great, then only one or

    tw o

    values need

    to be

    taken during

    the

    potential survey. Success-

    ful survey s ha ve often been made w ith only

    the

    value

    at the

    start

    and

    finish (together with those taken during

    the

    polarization ru n).

    These values should also be plotted in the field.

    5. Line current survey. If

    spaced p airs

    of

    test leads

    are

    available,

    th e

    line current should

    be

    determined

    oneach

    side

    of the

    drainage

    point ,and a t aremote locationineach dire ction . Interm ediate val-

    ues may

    also

    be useful ,

    part icular ly

    if it

    turns

    out

    that there

    are

    some short-circuited structures on the line. Like the potential

    readings,

    these

    should consist

    of on - off pairs.

    6.

    Repeat as necessary.

    New drainage points are chosen, and the

    outlined

    process repeated

    unti l the

    entire line

    has

    been covered

    with

    values large enou ghto beusable.It is by nomeans necessary

    to

    achieve complete protection over

    th e

    whole line,

    or

    even over

    any

    portion thereof.

    Graphical

    Presentationof Data

    Allof the

    info rm ation gathered

    in the

    survey should then

    be

    prepared

    in

    the

    form

    of a set of curves, as follows:

    1. Current

    and

    polarization.For

    each test run,

    th e

    value

    o f

    drainage

    current and the

    potential

    at the

    check point should

    be

    plotted

    against

    time (see Figure 4-2). The curve will have many points

    close together duringtheearly polarization ru n ,andperhaps only

    one or two

    thereafter,

    but

    should always

    be

    plotted

    as a

    complete

    curve.This

    wil l

    makei tpossible tointerpolateandth us determine

    th e

    value

    of the

    current f low ing

    at any

    particular time,

    tocorrelate

    with the

    various potential readings.

    2. Longitudinal distributioncurves.On a

    single cu rve,

    the following

    should

    beplotted against distance alongth e entire line : staticpo-

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    Figure

    4-2.

    Longitudinaldistributioncurves.

    Distributionof

    pipe-to-soil

    potentialalongtheline;thevery obviousdifference betweenthe two

    ends of theline

    illustrated

    are

    attributable

    to ashort-circuitedbare cas-

    ing on the

    right-hand

    section. The

    horizontal

    unitis 1000

    feet.

    tential, off potential, on potential,

    and

    line current.

    There

    will

    be only one static curve, but there will be one of each of the

    others for each test run. Normally, these will overlap, and colors

    may

    be required for clear separation. These curves will present

    most

    of the

    data taken

    in the field in

    graphic

    form.

    3.

    Attenuation

    curve.

    Again

    on a

    single sheet (Figure

    4-3),

    but

    using

    semilogarithmic paper,

    th e

    following

    are

    plotted against distance

    (using the samehorizontal scale as

    above):

    a. Polarization potential, AV>; this is the difference between the

    off potential and the static potential, at each point.

    b. Driving voltage,

    AE;

    this is thedifference between the on

    potential and the off potential, at each point.

    c. Line current,A/;again th evalueto beplotted is thedifference

    in

    th e

    on value

    and the

    off value;

    due

    attention must

    be

    paid

    to thedirections,an d thealgebraic

    difference taken. That

    is, if the

    test shows

    40

    m illiamperes flow ing east during off conditions

    and300 milliamperes flowing west during the on part of the

    cycle, then A / is 340 milliamperes, the net change produced by

    the test current.

    40 Pipeline Corrosion

    and Cathodic

    Protection

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    Current Requirement Surveys

    41

    Figure 4 3.Attenuation curves. Driving

    voltage AE) and

    polarization

    potential

    AV

    P

    )

    plottedonsemilog paper against distance alongtheline.

    For

    an

    infinitely long

    line,

    such curves should

    be

    straight lines;

    for a fi-

    nitelineendingin aninsulated joint, concave upward,as on theleft-

    handsection;and for a"grounded"section, concave downward,as on

    the right-hand section.Thetest point numberson allthree figures corre-

    spond.

    4. Polarization chart (Figure 4-4). Thisisusually plottedonlog-log

    paper, although

    the

    results

    are

    often

    as

    good when ordinary linear

    paper

    is

    used. This

    is a

    plot

    of the

    value

    of

    A V / > plotted against

    A, and, where several tests have been

    run on the

    same line,

    or

    even where there have been repeat tests

    on the

    same section with

    thesameo r

    different

    current values, allpairs

    from

    alltests can be

    combined. In general, it wi l l not beadvisable to combine values

    taken

    on

    different lines

    or on

    different sections

    if it is

    known that

    pipe size, line age,

    or

    type

    of

    coating

    is

    markedly different. This

    chart wil l usually

    be a scatter

    diagram rather than

    a

    smooth

    curve; often it isadvisable todraw limiting lines rather thanasin-

    gle

    curve through

    the

    points.

    The

    chart shown

    in

    Figure

    4-4 is

    bet-

    ter

    than most

    in the

    degree

    of

    conformity

    to a

    single curve.

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    Figure4-4.Polarization chart.Fromthisplot,the functionalrelationship

    betweendriving voltageandpolarization potential may beobtained.

    Test point 2 is

    anomalous.

    Theexplanation is found in the short-cir-

    cuited

    casing

    at

    this

    location,

    which

    minimized

    polarization. The

    anom-

    aly atpoint8 is due to

    proximity

    to the anode; the apparent value of the

    drivingvoltage

    is toohigh.

    Current

    Sources for Tests

    Whereverylargecurrents20-100amperesarerequired, aw eld-

    in g

    machine

    is the

    usual source

    of DC

    power

    for

    current requirement

    tests. Smaller values can be supplied by storage batteries. It is possible

    to

    connect

    any

    number

    of

    such batteries

    inseriesto

    obtain voltages high

    enough

    for medium-to-high

    resistance ground beds.

    As

    high

    as 120

    volts (ten 12-volt batteries)

    has

    been used with success.

    Very

    small currents, u p to perhaps two am peres, can be suppliedwith

    ordinary

    dry

    cells, often

    at a

    considerable saving

    in

    cost,

    if no

    storage

    battery

    is

    rea