Short Course _Thermodynmics

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  • 8/12/2019 Short Course _Thermodynmics

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    To be a partner of choice in corro

    research

    orrosion Thermodynamics

    5/27/2014 1Corrosion Electrochemistry :

    Thermodynamics

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    Thermodynamics deals with energy and itschanges in reactions.

    Reactions are viewed in terms of changes in freeenergy.

    According to the first law of thermodynamicsenergy can be neither created nor destroyed.

    The second law states that the free energy isreleased from the system to surroundings in allspontaneous changes.

    Corrosion reactions are spontaneous and aregoverned by the laws of thermodynamics.

    2

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    Tendency to corrode and rate of corrosion

    Tendency to corrodeis determined by the free energy difference

    between a metal and its corrosion product.

    Consider the reaction:

    Rate of corrosionis determined by the size of the energy barrier, the free energy of

    activation,

    G

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    For the forward reaction the temperature dependence is given by theArrhenius equation.

    A= undefined constant; R= gas constant, T= absolute temperature

    The relationship between free energy and equilibrium constant for a

    reaction:

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    For a spontaneous transition from high energy(initial

    state, Gi) to low energy (final state, Gf), the free energy

    change

    G = Gf- Gi< 0 (negative)

    For a spontaneous reaction to occur, Gmust benegative !

    .Mg + H2O + O2 = Mg(OH)2 (

    G

    o

    = -596 kJ/mol)Cu + H2O + O2 = Cu(OH)2 (G o= -119 kJ/mol)

    Au + 3/2H2O + O2 = Au(OH)3 (G o= +66 kJ/mol)

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    Nernst equation

    The free energy change is related to electrical potential by

    Faraday's law:

    G=

    nFE and G=

    nFE

    Where, F=Faraday constant, 96,500 coulombs/mole; n

    number of electrons transferred in the corrosion reaction and

    E is the measured potential in volts.

    Under standard conditions, G= -nFEo

    From G = G+ (RT)ln{[C][D]/{[A][B]},

    we have

    - nFE= -nFEo+ (RT)ln{[C][D]}/{[A][B],the Nernst equation:

    E= Eo- (RT/nF)ln{[[C][D]}/{[A][B]}

    This is one of the most fundamental equations incorrosion science and engineering.

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    Under standard conditions: T=298k, R=8.3143 J (mol k)-1,

    ln X = 2.3 logX

    Nernst equation can be written as

    E= Eo- (0.059/z)log{[Products]/[Reactants]}

    E is the non equilibrium potential generated by the corrosionreaction;

    [reactants] = concentration of reactants and

    [products] = concentration of products.

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    Standard Electrode Potentials

    The potential difference between the anode and cathode can be

    measured by voltage measuring device. The absolute potential of the

    anode and cathode cannot be measured directly.

    To define a standard electrode, all other potential measurements are

    made against the standard electrode. If the standard electrode

    potential is arbitrarily set to zero, the potential difference measured

    can be considered as the absolute potential.

    Standard Hydrogen ElectrodeThe half-cell in which the hydrogen reaction takes place is called the

    standard hydrogen electrode, often abbreviated SHE

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    Electrode Standard Electrode Potential,EoV

    (SHE)

    Au3++ 3e-= Au + 1.50

    Cl2 + 2e- = 2Cl- + 1.360

    O2+ 2H++ 2e = H2O + 1.228Br2+ 2e = 2Br

    _ + 1.065

    Ag++ e = Ag + 0.799

    Hg22++ 2e = 2Hg + 0.789

    Fe2++ e_= Fe3+ + 0.771

    I2+ 2e = 2I-

    + 0.536Cu++ e = Cu + 0.520

    Cu2++ 2e = Cu + 0.337

    2H++ 2e = H2 0.000 (by definition)

    Pb2++ 2e = Pb 0.126

    Sn2++ 2e = Sn 0.136

    Ni2++ 2e = Ni 0.250

    Fe2++ 2e = Fe 0.440

    Cr3++ 3e = Cr 0.740

    Zn2++ 2e = Zn 0.763

    Al3++ 3e = Al 1.663

    Mg2++ 2e = Mg

    2.370+ + =

    The logical choice

    is for all reactants

    in their standard

    states and

    potentials for this

    condition are

    described asstandard

    electrode

    potent ials, Eo.

    Noble

    or

    Cathodic

    Activeor

    Anodic

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    Standard Electrode Potential

    The potential difference measured between metal, M, and the

    hydrogen electrode, under well defined conditions.

    Example:

    Iron corrodes in a solution of H+

    (a) iron dissolves: half-cell reaction: Fe = Fe2++ 2e-(b) hydrogen gas formed: half-cell reaction: 2H++ 2e- = H2

    (c) overall reaction: corrosion reaction: Fe + 2H+= Fe2++ H2

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    Substituting into Nernst equation:

    E=Eo- (0.059/2)lg{[Fe2+][H2]/[Fe][H+]2}

    The terms [H+] and [H2] have been made to 1, [Fe] can be

    approximated as unity, so under standard conditions, [Fe2+] = 1 M,

    E= Eo

    The measured potential difference is the electrode potential of the

    iron under standard conditions.

    Points to note: if the measured potential is positive

    dG=-nFE < 0, spontaneous reaction.

    Eo= + 0.44 V, dG is negative, iron corrodes spontaneously in acid.

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    The Basic Wet Corrosion Cell

    Four essential components of a corrosion cell

    The Anode

    The Cathode

    The Ionic Conductor (electrolyte)

    The Metallic Conductor (electrical connection)

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    (1) The anode

    The anode corrodes by loss of electrons: M= Mz++ ze-

    Anodic reaction

    Oxidation reaction

    Electron generation

    (2) The cathode

    The cathode does not corrode. Most important cathodic reactions:(i) pH < 7 2H++ 2e- =H2

    (ii) pH > = 7 2H2O + O2+ 4e- = 4OH-

    Other cathodic reactions are possible Depending on the environment.Cathode

    Cathodic reaction

    Reduction reaction

    Electron consumption

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    3) An electrolyte (ionic conductor)

    a solution conducting electricity

    (4) Electrical connection

    the anode and cathode in a corrosion cell must be in electrical contact.Difference in free energies between the anode and the cathode

    produces electrical potential which is the driving force for corrosion

    reaction.

    Current: flow of electrons; Corrosion current:corrosion rate

    Points to note: all aqueous corrosion reactions can bethought of in

    terms of the simple corrosion cell.

    Separation of anode and cathode

    permanent separation

    differential aeration

    random distribution

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    Cell Potential

    Dry batteries and Daniell cell

    Symbolism of a corrosion cell: Zn | Zn2+|| Cu2+| Cu

    Zn electrode on the left, immersed in Zn2+ions; Cu electrode on

    the right, immersed in Cu2+

    ions. Ionic species are separated by || .Zinc is the anode, copper is the cathode.

    The two half-cell reactions are:

    Zn = Zn2++ 2e-

    Cu2++ 2e- = Cu

    The overall reaction Zn + Cu2+= Zn2++ Cu

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    To find the theoretical cell potential, using Nernst equation for each

    of the half-cell reactions:

    E(Zn/Zn2+)=Eo(Zn/Zn2+) - (0.059/2)lg[Zn2+], andE(Cu2+/Cu)=Eo(Cu2+/Cu) - (0.059/2)lg{1/[Cu2+]}.

    So the cell potential

    E(cell)=Eo(cell) - (0.059/2)lg{[Zn2+]/[Cu2+]}

    Convention:

    do not use oxidation potential

    do use reduction potential

    Eo(cell) = Eo(cathode) + Eo(anode)