05-Experimental Polarization Curves

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    EXPERIMENTAL POLARIZATION CURVES

    Dr. Ramazan Kahraman

    Chemical Engineering Department

    King Fahd University of Petroleum & MineralsDhahran, Saudi Arabia

    Reading Material: Chapter 3, Sections 3.4 and 3.5 in

    Principles and Prevention of Corrosion, Denny Jones, Prentice-Hall, 1996.

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    Increase cathodic polarization by c (from c=Ecorr-ec to c=E*-ec) and

    plot applied current, iapp, vs potential, E.

    (Same principle is applied in cathodic protection which is to be studied later)

    [Principles and Prevention of Corrosion, Denny Jones, Prentice-Hall, 1996]

    Cathodic Polarization(Polarization of cathodic rxn by shift of potential to a more negative value)

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    Anodic Polarization

    (Polarization of anodic rxn by shift of potential to a more positive value)

    Increase anodic polarization by a (from a=Ecorr-ea to a=E*-ea) and

    plot applied current, iapp, vs potential, E.

    (Same principle is applied in anodic protection (in the case of

    active-passive metals) which is to be studied later)

    ic + iapp = iasupplies e- consumes e-*

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    Experimental Polarization Curves

    [Principles and Prevention of Corrosion, Denny Jones, Prentice-Hall, 1996]

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    Non-ideal Experimental Polarization Curves

    Use of cathodic polarization data to form the anodic polarization curve in the case ofnon-linear anodic data (distorted probably by corrosion products at high currents).

    ia = ic - iapp

    Cathodic Polarization

    [Principles and Prevention of Corrosion, Denny Jones, Prentice-Hall, 1996]

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    Instrumentation

    Controlled current (galvanostatic) technique

    [Principles and Prevention of Corrosion, Denny Jones, Prentice-Hall, 1996]

    Current is applied at a

    pre-determined rateand the potential is

    measured through a

    reference electrode

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    Instrumentation

    Controlled potential (potentiostatic) technique

    [Principles and Prevention of Corrosion, Denny Jones, Prentice-Hall, 1996]

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    Reactions on the Auxiliary Anode

    During Cathodic Polarization

    For the working electrode as an anode, metal dissolution reactions of the type

    M Mn+ + ne- (1)

    are of interest in corrosion.

    When the working electrode is polarized as cathode (auxiliary electrode as anode),

    M must be selected for the auxiliary electrode with a very noble eM/Mn+ to prevent

    anodic dissolution, which would contaminate the electrolyte. Either platinum orcarbon/graphite is the usual choice.

    In the absence of anodic dissolution at the auxiliary electrode by reaction (1), other

    anodic oxidation reactions are possible to liberate electrons. These include

    oxidation in a redox reaction such asFe2+ Fe3+ + e- (2)

    And oxygen evolution by

    4OH- 2H2O + O2 + 4e- (3)

    Reactions (2) and (3) both must operate at potentials below eM/Mn+ (e.g. ePt/Pt3+) so

    that nobel-metal auxiliary electrode is not dissolved.

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    Home Work Problems

    Prbs. 10 and 11 of Ch.3in Principles and Prevention of Corrosion, Denny Jones, Prentice-Hall, 1996.

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    References

    Principles and Prevention of Corrosion, Denny Jones, Prentice-Hall, 1996.