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    Corrosion Engineering

    N Balasubramanian

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    CHE3166: Materials and Corrosion

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    Corrosion:Corrosion: ?

    Corrosion: Destruction of a material by reactionCorrosion: Destruction of a material by reaction

    with its environment.with its environment.

    Corrodere (Latin)Corrodere (Latin) -- To Eat AwayTo Eat Away

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    The basic corrosion reaction

    M M+ + e-

    e a ecomes a ca on

    Oxidation reaction

    Electrochemical reaction

    Need to have a corresponding reduction

    reaction

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    Categories

    Infrastructure

    Utilities

    Cost of Corrosion

    Transportation

    Production & Manufacturing

    Government

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    Motor Vehicles 23.4

    Ships 2.7

    Aircraft 2.2

    Oil & Gas Exploration & Production 1.4

    Mining 0.1

    Petroleum Refining 3.7

    Chemical, Petrochemical, & Pharmaceutical 1.7

    Cost of Corrosion

    Railroad Cars 0.5

    Hazardous Materials Transport 0.9

    TOTAL: 29.7

    Pulp & Paper 6.0

    Agricultural Production 1.1

    Food Processing 1.1

    Electronics -

    Home Appliances 1.5

    TOTAL 17.6

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    Cost of Corrosion

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    The eight forms are:

    forms of corrosion

    5. intergranular corrosion. , ,

    2. galvanic, or two-metal corrosion,

    3. crevice corrosion,

    4.pitting

    6. selective leaching, or parting

    7. erosion corrosion, and

    8. stress corrosion.

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    Forms of Corrosion

    Uniform CorrosionUniform Corrosion

    Galvanic CorrosionGalvanic Corrosion

    Crevice CorrosionCrevice Corrosion

    ErosionErosion--corrosioncorrosion

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    Uniform Corrosion

    Uniform attack is the most common form of corrosion. It is normally

    characterized by a chemical or electrochemical reaction which

    proceeds uniformly over the entire exposed surface or over a large

    area. The metal becomes thinner and eventually fails. For example, a

    piece of steel or zinc immersed in dilute sulfuric acid will normally

    dissolve at a uniform rate over its entire surface. A sheet iron roof willshow essentiall the same de ree of rustin over its entire outside

    surface.

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    Forms Of Corrosion

    Uniform CorrosionUniform Corrosion

    Galvanic CorrosionGalvanic Corrosion

    PittingPitting

    Crevice CorrosionCrevice Corrosion

    ErosionErosion--corrosioncorrosion

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    Dissimilar Metal Couples

    GraphiteTitanium

    Alloy C-276

    Stainless Steel

    OK?

    Copper

    Cast Iron

    SteelAluminum

    Zinc

    OK

    Can BeBad

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    Galvanic Corrosion

    A potential difference usually exists between two dissimilar metals

    when they are immersed in a corrosive or conductive solution. If these

    metals are placed in contact (or otherwise electrically connected), this

    potential difference produces electron flow between them. Corrosion of

    the less corrosion-resistant metal is usually increased and attack of the,

    these metals when they are not in contact. The less resistant metal

    becomes anodic and the more resistant metal cathodic. Usually the-

    cathode or cathodic metal corrodes very little or not at all in this type of

    couple. Because of the electric currents and dissimilar metals involved,

    this form of corrosion is called galvanic, or two-metal, corrosion. It is

    electrochemical corrosion, but we shall restrict the term galvanic to

    dissimilar-metal effects for purposes of clarity.

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    Galvanic Corrosion

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    Forms Of Corrosion

    Uniform CorrosionUniform Corrosion Galvanic CorrosionGalvanic Corrosion

    PittingPitting

    Crevice CorrosionCrevice Corrosion ros onros on--corros oncorros on

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    Pitting Corrosion

    Pitting is a form of extremely localized attack that results in holes in the

    metal. These holes may be small or large in diameter, but in most cases they

    are relatively small. Pits are sometimes isolated or so close together that

    they look like a rough surface. Generally a pit may be described as a cavity

    or hole with the surface diameter about the same as or less than the depth.

    Pitting is one of the most destructive and insidious forms of corrosion. It

    weight loss of the entire structure. It is often difficult to detect pits because

    of their small size and because the pits are often covered with corrosion

    products. In addition, it is difficult to measure quantitatively and compare

    the extent of pitting because of the varying depths and numbers of pits that

    may occur under identical conditions.

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    Pitting Corrosion

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    Forms of Corrosion

    Uniform CorrosionUniform Corrosion Galvanic CorrosionGalvanic Corrosion

    PittingPitting

    Crevice CorrosionCrevice Corrosion

    ErosionErosion--corrosioncorrosion

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    Crevice Corrosion

    Intense localized corrosion frequently occurs within crevices and other shielded

    areas on metal surfaces exposed to corrosives. This type of attack is usually

    associated with small volumes of stagnant solution caused by holes, gasket

    surfaces, lap joints, surface deposits, and crevices under bolt and rivet heads. As a

    result, this form of corrosion is called crevice corrosion or, sometimes, deposit or

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    Crevice Corrosion

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    Forms Of Corrosion

    Erosion corrosion is the acceleration or increase in rate of deterioration or

    attack on a metal because of relative movement between a corrosive fluid and

    the metal surface. Generally, this movement is quite rapid, and mechanical

    wear effects or abrasion are involved. Metal is removed from the surface as

    dissolved ions, or it forms solid corrosion products which are mechanically

    swept from the metal surface. Sometimes, movement of the environment

    Uniform CorrosionUniform Corrosion Galvanic CorrosionGalvanic Corrosion PittingPitting

    Crevice CorrosionCrevice Corrosion

    ErosionErosion--corrosioncorrosion

    ,

    conditions, but this is not erosion corrosion because deterioration is not

    increased.

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    Erosion-corrosion

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    Forms of Corrosion

    Selective leaching is the removal of one element from a solid alloy by corrosion

    processes. The most common example is the selective removal of zinc in brass

    alloys (dezincification). Similar processes occur in other alloy systems in which

    aluminum; iron, cobalt, chromium, and other elements are removed. Selective

    leaching is the general term to describe these processes, and its use precludes

    the creation of terms such as dealuminumification, decobaltification, etc. Parting is

    Selective LeachingSelective Leaching Intergranular Attack

    Corrosion Fatigue

    Environmental

    Cracking

    , .

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    Selective Leaching

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    Forms Of Corrosion

    Grain boundary effects are of little or no consequence in most applications

    or uses of metals. If a metal corrodes, uniform attack results since grain

    boundaries are usually only slightly more reactive than the matrix.

    However, under certain conditions, grain interfaces are very reactive and

    intergranular corrosion results. Localized attack at and adjacent to grain

    boundaries, with relatively little corrosion of the grains, is intergranular

    corrosion. The alloy disintegrates (grains fall out) and/or loses its strength.

    Selective Leaching

    Intergranular Attack (IGA)Intergranular Attack (IGA)

    Corrosion Fatigue

    Environmental Cracking26

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    Intergranular Corrosion

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    Intergranular Corrosion

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    Corrosion Fatigue

    60

    80

    100

    120

    ksi

    )

    ksi

    )

    0

    20

    40

    10,000 100,000 1,000,000 10,000,000 100,000,000

    In AirIn Air In SeawaterIn Seawater

    Stress

    Stress

    Cycles to FailureCycles to Failure

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    Corrosion Fatigue Fracture

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    Stress Corrosion Cracking

    Alloy Susceptible

    Tensile Stress

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    Stress Corrosion Cracking

    Vertical Heat Exchanger

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    Stress Corrosion Cracking

    Caustic Carryover In Steam

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    Forms of Corrosion

    Erosion corrosion is the acceleration or increase in rate of deterioration or

    attack on a metal because of relative movement between a corrosive fluid

    and the metal surface. Generally, this movement is quite rapid, and

    mechanical wear effects or abrasion are involved. Metal is removed from the

    surface as dissolved ions, or it forms solid corrosion products which are

    mechanically swept from the metal surface. Sometimes, movement of the

    Selective Leaching Intergranular Attack

    Corrosion Fatigue

    Environmental CrackingEnvironmental Cracking

    ,

    under stagnant conditions, but this is not erosion corrosion because

    deterioration is not increased.

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    Factors Favoring

    SCC Stainless Steels

    Temperature > 55 C

    Chlorides

    Evaporative Conditions

    Pit - Stress Raiser

    Residual Or Applied Stress

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    Mechanical And Physical Factors

    Strength, Ductility

    Formability

    ,

    Thermal Conductivity

    Thermal Expansion

    Unique Properties

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    Other Factors

    Safety

    Compatibility

    Cost

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    Economics

    Managements Language Is EconomicsManagements Language Is Economics

    Use Life Cycle Costs To Compare MaterialsUse Life Cycle Costs To Compare Materials

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    Materials Selection

    Define Environment

    Define Required Equipment Define Test And Inspection

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    Define Environment

    Major Reactants

    Minor Ingredients

    pH, Contaminants, Aeration

    Process Conditions

    Temperature, Pressure, Excursions

    Catalytic/inhibitive Effects

    e.g., Metallic Ions

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    Define Equipment

    Pressure Vessels

    Valves And Piping

    Tankage es ys ems

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    Test & Inspection

    Fabrication Verify Materials, Workmanship, Dimensions,

    Storage Conditions

    Testing & Inspection

    Develop Program

    Consider Corrosion Test Locations

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    Dont Expect Inspect

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    CHE3166Corrosion: Thermodynamics

    Net reaction is oxidation of zinc by copper(II) ions:

    Zn(s) + Cu2+ Zn2+ + Cu(s)

    Half reactions take place in separate locations:

    Left electrode: Zn(s) Zn2+ + 2e oxidation

    Right electrode: Cu2++ 2e Cu(s) reduction

    Electrochemical cells allow measurement and control of a redox (reduction/oxidation)

    reaction. Also, we can force the reaction to proceed in its non-spontaneous, or reversedirection by connecting a source of current to the two electrodes.

    To sustain the cell reaction, the charge carried by the electrons through the external

    circuit must be accompanied by a compensating transport of ions between the two cells.

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    To sustain the cell reaction, the charge carried by

    the electrons through the external circuit must be

    accompanied by a compensating transport of ions

    between the two cells.

    Relative amounts of charge can be carried by

    Galvanic cells and electrodes

    negat ve or pos t ve ons epen s on t e r re at ve

    mobilities) through the solution.

    Salt bridge, consists of an intermediate

    compartment filled with saturated salt solution and

    fitted with porous barriers at each end, is used forprecise measurements. The purpose of salt bridge is

    to minimize the natural potential difference

    (junction potential).

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    Consider zinc in a solution of hydrochloric acid

    Thermodynamics

    Zn + 2 ClZnCl2+H2

    This reaction can be separated into two half-cell reactions

    n n + e

    2H+ + 2e H2

    potential ea)

    Reduction reaction (cathodic reaction withpotential ec)

    has an associated free-energy change (G)

    G= nFE= nF ea+ ec( )

    n=number of electrons exchanged, F=96500 C/e-, E=potential

    Nernst Equation

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    Standard hydrogen electrode

    Pt is inert and acts as

    catalyst site

    1 atm H2 gas is the standards a e

    Solid Zn and 1N Zn2+ is the standard state

    Measured potential difference V is 0.762V

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    Standard hydrogen electrode

    For a pure Cu electrode in a

    1 N Cu 2+ solution, the

    potential difference in this

    cell is 1.104 V

    Zn2+ + 2e Zn 0.762V( )

    Cu2+

    + 2e

    Cu +0.342V( )

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    Electromotive Force Series

    Zn + 2HClZnCl2+ 2

    or

    ZnZn2+ + 2e

    2H+ + 2e H2

    = ea + ec

    E= +0.762 + 0

    = +0.762V

    G= nFE< 0

    At standard state, reaction

    will occur

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    Electromotive Force Series

    The half-cell reaction with the

    more active (negative) half-

    cell potential always proceeds

    as an oxidation, and thereaction with the more noble

    half-cell potential always

    proceeds as a reduction in the

    spontaneous reaction

    produced by the pairShipboard corrosion

    protection

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    Electromotive Force Series

    Question. Is copper (Cu)

    oxidized (dissolved) by ferric

    (Fe3+) ions?

    Ferric reduction is noble relative

    to copper so copper is oxidized

    (copper becomes an ion and

    gives off electrons)

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    Reaction Direction

    Written as reduction

    reactions from left to right

    y rogen re uc on s

    chosen (arbitrarily) as the

    reference and assigned

    zero potential

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    Standard conditions

    Standard states:

    For a solid, the solid is taken as unit activity

    For a gas, 1 atm pressure is taken as unit activity

    For dilute or strongly dissociated solutes typically found in

    most instances of corrosion, activity is reasonably approximated

    A( ) = CA

    A=activity of atom A= activity coefficient (tabulated)

    CA=concentration (g/l) of atom A

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    Activities

    Gases A=p (partial pressure in atm)

    Pure li uids and solids A=1

    Solutes A=M (molarity)

    Liquids in solutions A=X (mole fraction)

    Solvent in dilute solution A=1

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    Non-standard conditions

    Analyze a general half-cell equation between atom A and atom B in

    an aqueous solution

    aA +mH+ +ne = bB +dH2O

    or reac an s an pro uc s n e s an ar s a e

    G0 = bGB0 +dGH2O

    0( ) aGA0 +mGH+0( )

    For reactants and products in a non-standard state

    G= bGB +dGH2O( ) aGA +mGH+( )59

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    Non-standard conditions

    The departure of free energy in the non-standard state from the

    standard state is:

    G G0 = b GB GB0( )+d GH2O GH2O

    0( )[ ] a GA GA0( )+m GH+ GH+0( )[ ]

    The corrected concentration A available for the reaction is known as

    the activity of A and is given by:

    a GA GA0( )=aRTln(A) =RTlnA( )

    a

    G G0 =RTln B( )

    bH2O( )

    d

    A( )a

    H+( )m

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    Nernst Equation

    G G0 =RTln B( )

    bH2O( )

    d

    A( )a

    H+( )m

    = 0 RT B( )b

    H2O( )d

    G= nFE= nF ea + ec( )Recall

    2.3 T = 0.059

    At 25C

    nF A( )a

    H+( )m

    e= e0 +2.3RT

    nFlog

    A( )a

    H+( )m

    B( )b

    H2O( )d

    e= e0 +0.059

    nlog

    A( )a

    B( )b

    m

    n0.059pH

    pH= logH+( )

    Recall

    Activity of water=1 for

    aqueous solutions

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    Electrochemical potential

    e= e0 +0.059

    nlog

    A( )a

    B( )b

    m

    n0.059pH

    Examine specific half-cell reactions

    + e = 2

    eH+ /H2

    = eH+ /H2

    0 0.059pH

    ,

    so activity=1

    As the activity of any dissolved oxidizer (e.g., H+) increases,

    more noble or positive potentials are routinely measured

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    Electrochemical potential

    The above reaction occurs in an acid solution. An

    equivalent reaction in neutral or alkaline solutions is:

    2H+ + 2e =H2 eH+ /H2 = eH+ /H20

    0.059pH

    0

    The electrochemical evolution of hydrogen is the

    decomposition of water

    2 + e = 2+ eH+ /H2= e

    H+ /H2 . p

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    Potential/pH (Pourbaix) Diagram

    eH+ /H2

    = eH+ /H2

    0 0.059pH

    oxygen evolution

    and acidification

    For hydrogen evolution at a fixedpotential

    2H+

    + 2e

    =H2

    + hydrogen evolution

    and alkalization

    decreases), we are less likely to

    form H2 gas

    Note that, consistent with the half-cell potential definitions,

    the hydrogen line goes through zero potential at zero pH

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    Potential/pH (Pourbaix) Diagram

    oxygen evolution

    and acidification

    At higher potential

    O2+ 4H+

    + 4e

    2H2O

    is feasible

    eO2 /H2O = eO2 /H2O 0.059pHhydrogen evolutionand alkalization

    Note that, consistent with the half-cell potential definitions,the oxygen line goes through 1.229V at zero pH and 0.401V atpH=14.

    This reaction is the basis for water electrolysis65

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    Potential/pH (Pourbaix) Diagram

    Corrosion-soluble ions of the

    metal are stable

    Passivation- oxides are stable

    Immunity-reduced form of the

    metal is stable

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    Potential/pH (Pourbaix) Diagram

    Reaction 1: Metal oxidizes to

    aqueous cations

    Pourbaix diagram for Al

    M=Mn +

    +ne

    l= l3+ + 3e

    eAl/Al3+

    = e0 +0.059

    nlog

    A( )a

    B( )b

    m

    n0.059pH

    eAl/Al3+

    = 1.662 +0.059

    3logAl3+( )

    Independent of pH since

    no H+ is involved.

    Only depends on Al3+

    activity

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    Potential/pH (Pourbaix) Diagram

    Reaction 2: Metal reacts to metal

    hydroxide or oxide

    Pourbaix diagram for Al

    M+nH2O =M OH( )n+nH+ +ne

    +

    2 = 2 3 e

    eAl/Al2O3 = 1.55 0.059pH

    At higher pH Al2O3 is formed. At lower pH Al2O3 dissolves to Al3+

    Intersection depends depends on Al3+ activity (dashed lines areportions of the reactions with no significance)

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    Potential/pH (Pourbaix) Diagram

    The reaction rate constant for

    Pourbaix diagram for Al

    2Al3+

    + 3H2O =Al2O3+ 6H+

    K=H+( )

    6

    Al3+( )2

    = 1011.4

    For (Al3+)=10-6,

    logK= 6logH+( ) 2log Al3+( )= 6pH 2log Al3+( )

    pH= 3.9 Independent of potential

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    Potential/pH (Pourbaix) Diagram

    Reaction 3: Metal reacts to form

    soluble aqueous anions

    Pourbaix diagram for Al

    = n2m + m

    Al+ 2H2O =AlO2 + 4H+ + 3e

    eAl/AlO2

    = eAl/AlO2

    0 +0.059

    3logAlO2

    ( )

    4

    30.059pH

    eAl/AlO2

    = 1.262 + 0.020log AlO2( ) 0.079pH

    At higher pH, Al2O3 dissolves to AlO2-

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    P b i Di F

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    Pourbaix Diagram Fe

    Example 2: stability diagram for iron (little

    bit complicated).

    Horizontal lines: reactions areinvolved with electrons (potential),

    but independent of pH (H(+a) or OH(-a)

    ions):

    Fe2+=Fe3++e

    Ee=0.771+0.0591lg(aFe3+/aFe

    2+)

    Fe=Fe2++2e

    Ee=0.771+0.0591lg(aFe3+/aFe

    2+)

    Vertical lines: reactions are

    involved with pH, but independent of

    electrons:

    Fe3++H2O=FeOH2++H+

    lg(aFeOH2+/aFe

    3+)=-2.22+pH

    Fe2++2H2O=Fe(OH)2+2H+

    lg(aFe2+)=13.37-2pH

    Diagonal lines: reactions are

    involved both pH and electrons:

    Fe2++H2O=FeOH2++H++eEe=0.877-0.0591pH+0.0591lg(aFe(OH)

    2+/aFe2+)

    Fe2++3H2O=Fe(OH)3+3H++e

    Ee=0.748-0.1773pH-0.0591lgaFe2+

    Fe+2H2O=Fe(OH)2+2H++2e

    Ee=-0.045-0.0591pH

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    Standard Hydrogen Electrode

    Platinum Foil suspended in

    sulfuric acid with unit activity of

    H+. Platinum is noble and does

    not participate (acts as catalyst

    Connected to another half-cell

    through a solution bridge that

    allows for charge but not masstransfer

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    Ohter Electrodes

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    Questions?

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