Lecture 8 Electro-Kinetics

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    Electro-Kinetics

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    Description of Electrochemical

    Techniques

    The technique is named according to theparameters measured

    E.g.

    Voltammetry measure current and voltage

    Potentiometry measure voltage

    Chrono-potentiometry measure voltage with

    time (under an applied current) Chrono-amperometry measure current with

    time (under an applied voltage)

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    Electro-Kinetics

    Movement of Ions

    Butler Volmer Equation

    Rotating Disc Electrode

    Rotating Cylinder Electrode

    Voltammetry

    Cyclic Voltammetry

    Chrono-potentiometry

    Chrono-amperometry

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    Movement of Ions in Solution

    Diffusion Movement under a concentration gradient. If

    an electrochemical reaction occurs the current due to

    this reaction is called, id , the diffusion current.

    Migration or Transport Movement of ions under an

    electric field due to coulombic forces. If anelectrochemical reaction occurs the current due to this

    reaction is called, im , the migration current.

    Convection Movement due to changes in density at the

    electrode solution interface. This occurs due to depletionor addition of a species due to the electrochemical

    reaction.

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    The Capacitance Current

    The charging or capacitance current, ic , isdue to the

    presence of the electrical double layer and it is alwayspresent. This current, of course, is not related to any

    movement of ions.

    Ic = Cdl x V

    Where:

    Cdl = the capacitance of the electrical double layer

    V = voltage scan rate

    The capacitance current makes its presence felt whenmeasuring charge transfer (Faradaic) processes at

    concentrations of 10-5 M.

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    Diffusion

    Molecular diffusion,often called simplydiffusion, is a nettransport of

    molecules from aregion of higherconcentration to oneof lower

    concentration byrandom molecularmotion.

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    Migration or Transport

    Is the fraction of current carried by the ions.

    For example in a solution of copper sulphate the transportnumber of Cu2+ is 0.4 and that of SO4

    2- = 0.6.

    t++ t- = 0.4 + 0.6 = 1

    Since the migration current depends on the ionic strength of

    the solution it is usually eliminated by addition of excess of aninert supporting electrolyte (100 1000 fold excess inconcentration)

    The current is carried by the inert supporting electrolyte (e.g.NaCl , KNO

    3etc) because the ions produced do not undergo

    any electrochemical reaction the transport current iseffectively removed.

    In excess inert supporting electrolyte, the current measureddue to the electro-active species of interest is due only to

    diffusion which can be related to mass transfer.

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    Voltammetry the following example shows how the migration

    current is eliminated. Pb2+ + 2e Pb0

    The supporting electrolyte Ensures diffusion control of limiting currents by eliminating

    migration currents

    Table: Limiting currents observed for 9.5 x 10-4 M PbCl2 as a

    function of the concentration of KNO3 supporting electrolyte

    Molarity

    of KNO3

    IlA

    0 17.6

    0.001 12.0

    0.005 9.8

    0.10 8.45

    1.0 8.45

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    Voltammetry

    The example shown is for the reduction of Pb

    2+

    at aninert mercury electrode.

    Pb2+ + 2e Pb(Hg)

    At low inert electrolyte concentration a large fraction

    of the total current is due to the migration current,

    i.e. the currents due to the electrostatic attraction of

    ions to the electrode.

    For solution 1: i migration im 17.6 8.45 = 9.2 A

    i diffusion id = 8.45 A

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    Ficks First Law of Diffusion

    Fick's first law relates the diffusive flux to theconcentration field, by postulating that the flux goesfrom regions of high concentration to regions of lowconcentration, with a magnitude that is proportional

    to the concentration gradient (spatial derivative). Inone (spatial) dimension, this is

    x

    DJ

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    Ficks First Law of Diffusion

    where

    J is the diffusion flux in dimensions of [(concentration of

    substance) length2 time-1], example mole (M) m-2 s-1. J measures the amount of substance that will flow

    through a small area during a small time interval.

    D is the diffusion coefficient or diffusivity in dimensionsof [length2 time1], example m2 s-1

    (for ideal mixtures) is the concentration in dimensionsof [(concentration of substance) length3], example M m-3

    xis the position [length], example m

    xDJ

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    Ficks First Law of Diffusion

    D is proportional to the squared velocity of thediffusing particles, which depends on thetemperature, viscosity of the fluid and the size of theparticles according to the Stokes-Einstein

    relationship. In dilute aqueous solutions the diffusion coefficients

    of most ions are similar and have values that at roomtemperature are in the range of 0.6x10-9 to 2x10-9m2/s.

    For biological molecules the diffusion coefficientsnormally range from 10-11 to 10-10 m2/s.

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    Ficks First Law of Diffusion

    In two or more dimensions we must use, , the del orgradient operator, which generalises the first derivative,obtaining

    J = -D

    The driving force for the one-dimensional diffusion is thequantity -/x

    which for ideal mixtures is the concentration gradient. Inchemical systems other than ideal solutions or mixtures,the driving force for diffusion of each species is the

    gradient of chemical potential of this species. Then Fick'sfirst law (one-dimensional case) can be written as:

    xRT

    DcJ ii

    1

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    Ficks First Law of Diffusion

    where the index i denotes the ith species, c is the concentration (mol/m3),

    R is the universal gas constant (J/(K mol)),

    T is the absolute temperature (K), and

    is the chemical potential (J/mol).

    xRT

    DcJ ii

    1

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    Butler-Volmer Equation

    The Butler-Volmer equation is one of the

    most fundamental relationships in

    electrochemistry. It describes how the

    electrical current on an electrode depends onthe electrode potential, considering that both

    a cathodic and an anodic reaction occur on

    the same electrode:

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    Butler-Volmer Equation

    where:

    I = electrode current, Amps

    Io= exchange current density, Amp/m2

    E = electrode potential, V Eeq= equilibrium potential, V

    A = electrode active surface area, m2

    T = absolute temperature, K

    n = number of electrons involved in the electrode reaction

    F = Faraday constant R = universal gas constant

    = so-called symmetry factor or charge transfer coefficientdimensionless

    The equation is named after chemists John Alfred Valentine Butler and

    Max Volmer

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    Butler-Volmer Equation

    The equation describes two regions: At high overpotential the Butler-Volmer equation

    simplifies to the Tafel equation

    E Eeq = a blog(ic) for a cathodic reaction

    E Eeq = a + blog(ia) for an anodic reaction

    Where:

    a and b are constants (for a given reaction and

    temperature) and are called the Tafel equationconstants

    At low overpotential the Stern Geary equation

    applies

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    Current Voltage Curves for Electrode Reactions

    Without concentrationand therefore masstransport effects tocomplicate theelectrolysis it is possibleto establish the effects of

    voltage on the currentflowing. In this situationthe quantity E - Ee reflectsthe activation energyrequired to force current ito flow. Plotted below are

    three curves for differingvalues ofio with = 0.5.

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    Voltammetry

    Although the Butler Volmer Equation predicts, thatat high overpotential, the current will increaseexponentially with applied voltage, this is often notthe case as the current will be influenced by masstransfer control of the reactive species.

    Take the following example of the reduction of ferricions at a platinum rotating disc electrode (RDE).

    Fe3+ + e = Fe2+

    The rotation of the electrode establishes a welldefined diffusion layer (Nernst diffusion layer)

    The contribution of the capacitance current will alsobe demonstrated in this example.

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    Effect of the Capacitance Current in Voltammetry. The reduction of Ferric Chloride

    is carried out in the presence of 1 M NaCl to eliminate the migration current.

    Slope due to ic

    Applied Potential -Ve

    Current

    10-5 M Fe3+ Fe3+ + e Fe2+

    Current

    10-3 M Fe3+ Fe3+ + e Fe2+

    Applied Potential -Ve

    (a)

    (b)

    Note that the iE curve in Fig. (a)

    is recorded at a much higher

    sensitivity than in Fig. (b).

    ild

    ild

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    Charging Current or Capacitance

    Current

    Note that due to the presence of the electrical

    double layer a charging or capacitance current

    is always present in voltammetric

    measurements.

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    Butler-Volmer Equation

    where:

    I = electrode current, Amps

    Io= exchange current density, Amp/m2

    E = electrode potential, V

    Eeq= equilibrium potential, V

    A = electrode active surface area, m2

    T = absolute temperature, K

    n = number of electrons involved in the electrode reaction

    F = Faraday constant R = universal gas constant

    = so-called symmetry factor or charge transfer coefficientdimensionless

    The equation is named after chemists John Alfred Valentine Butler andMax Volmer

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    Butler Volmer Equation

    While the Butler-Volmer equation is valid over the fullpotential range, simpler approximate solutions can beobtained over more restricted ranges of potential. Asoverpotentials, either positive or negative, become largerthan about 0.05 V, the second or the first term of equation

    becomes negligible, respectively. Hence, simple exponentialrelationships between current (i.e., rate) and overpotentialare obtained, or the overpotential can be considered aslogarithmically dependent on the current density. Thistheoretical result is in agreement with the experimentalfindings of the German physical chemist Julius Tafel (1905),and the usual plots of overpotential versus log current densityare known as Tafel lines.

    The slope of a Tafel plot reveals the value of the transfercoefficient; for the given direction of the electrode reaction.

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    Butler-Volmer Equation

    ialoverpotentcathodichighat

    exp

    ialoverpotentanodichighat

    1exp

    0`

    0`

    RT

    nFii

    RTnFii

    cc

    aa

    ia and icare

    the exhange

    current

    densities for

    the anodicand cathodic

    reactions

    These equations can be rearranged to give

    the Tafel equation which was obtained

    experimentally

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    Butler Volmer Equation - Tafel Equation

    nb

    in

    a

    iba

    in

    in

    in

    in

    i

    nF

    RTi

    nF

    RT

    o

    aaa

    a

    c

    cc

    c

    c

    cc

    c

    059.0

    ln059.0

    and

    log

    equationTafelknownwelltheisequationThe

    processanodicfor theC25atlog059.0

    log059.0

    processcathodicfor theC25atlog059.0

    log059.0

    lnln

    0

    0

    0

    0

    0

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    Tafel Equation

    The Tafel slope is an intensive parameter and does not

    depend on the electrode surface area.

    i0 is and extensive parameter and is influenced by the

    electrode surface area and the kinetics or speed of the

    reaction.

    Notice that the Tafel slope is restricted to the number of

    electrons, n, involved in the charge transfer controlled

    reaction and the so called symmetry factor, .

    n is often = 1 and although the symmetry factor can varybetween 0 and 1 it is normally close to 0.5.

    This means that the Tafel slope should be close to 120

    mV if n = 1 and 60 mV if n = 2.

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    Tafel Equation

    We can write:

    ii

    nF

    RTb

    iibiinF

    RT

    log303.2ln

    slopeTafelthe303.2

    where

    lnorln 00

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    Current Voltage Curves for Electrode Reactions

    Without concentrationand therefore masstransport effects tocomplicate theelectrolysis it is possibleto establish the effects of

    voltage on the currentflowing. In this situationthe quantity E - Ee reflectsthe activation energyrequired to force current ito flow. Plotted below are

    three curves for differingvalues ofio with = 0.5.

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    Tafel Equation

    The Tafel equation can be also written as:

    where

    the plus sign under the exponent refers to an anodicreaction, and a minus sign to a cathodic reaction, n isthe number of electrons involved in the electrodereaction k is the rate constant for the electrodereaction, R is theuniversal gas constant, F is the

    Faraday constant. kis Boltzmann's constant, Tis theabsolute temperature, e is the electron charge, and is the so called "charge transfer coefficient", thevalue of which must be between 0 and 1.

    http://en.wikipedia.org/wiki/Faraday_constanthttp://en.wikipedia.org/wiki/Universal_gas_constanthttp://en.wikipedia.org/wiki/Boltzmann's_constanthttp://en.wikipedia.org/wiki/Boltzmann's_constanthttp://en.wikipedia.org/wiki/Absolute_temperaturehttp://en.wikipedia.org/wiki/Absolute_temperaturehttp://en.wikipedia.org/wiki/Absolute_temperaturehttp://en.wikipedia.org/wiki/Absolute_temperaturehttp://en.wikipedia.org/wiki/Boltzmann's_constanthttp://en.wikipedia.org/wiki/Electron_chargehttp://en.wikipedia.org/wiki/Electron_chargehttp://en.wikipedia.org/wiki/Electron_chargehttp://en.wikipedia.org/wiki/Electron_chargehttp://en.wikipedia.org/wiki/Absolute_temperaturehttp://en.wikipedia.org/wiki/Electron_chargehttp://en.wikipedia.org/wiki/Electron_chargehttp://en.wikipedia.org/wiki/Absolute_temperaturehttp://en.wikipedia.org/wiki/Boltzmann's_constanthttp://en.wikipedia.org/wiki/Faraday_constanthttp://en.wikipedia.org/wiki/Universal_gas_constant
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    Tafel Equation

    The following equation was obtainedexperimentally

    Where:

    = the over-potential

    i= the current density

    a and b = Tafel constants

    iba log

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    Tafel Equation

    Applicability

    Where an electrochemical reaction occurs in two half reactions onseparate electrodes, the Tafel equation is applied to each electrodeseparately.

    The Tafel equation assumes that the reverse reaction rate isnegligible compared to the forward reaction rate.

    The Tafel equation is applicable to the region where the values ofpolarization are high. At low values of polarization, the dependenceof current on polarization is usually linear (not logarithmic):

    This linear region is called "polarization resistance" due to its formalsimilarity to Ohms law

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    Stern Geary Equation Applicable in the linear region of the Butler Volmer

    Equation at low over-potentials

    resistanceonpolarisatimeasuredthe

    3.2

    constantTafelthe

    Where

    a

    a

    iE

    R

    B

    R

    Bi

    p

    c

    c

    p

    corr

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    Tafel Equation

    Overview of the terms

    The exchange current is the current at equilibrium,i.e. the rate at which oxidized and reduced speciestransfer electrons with the electrode. In other words,the exchange current density is the rate of reaction

    at the reversible potential (when the overpotential iszero by definition). At the reversible potential, thereaction is in equilibrium meaning that the forwardand reverse reactions progress at the same rates.This rate is the exchange current density.

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    Tafel Equation

    The Tafel slope is measured experimentally; however,

    it can be shown theoretically when the dominantreaction mechanism involves the transfer of a singleelectron that

    Tis the absolute temperature,

    R is the gas constant

    is the so called "charge transfer coefficient", thevalue of which must be between 0 and 1.

    FRTb

    303.2

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    Levich Equation

    The Levich Equation models the diffusion and solution

    flow conditions around a rotating disc electrode (RDE). Itis named after Veniamin Grigorievich Levich who firstdeveloped an RDE as a tool for electrochemical research.It can be used to predict the current observed at an RDE,in particular, the Levich equation gives the height of thesigmoidal wave observed in rotating disk voltammetry.The sigmoidal wave height is often called the Levichcurrent.

    In work at a RDE the electrode is usually rotated quite

    fast (1000 rpm) in order to establish a well defineddiffusion layer.

    The scan rate is relatively slow typically 2-5 mV s-1

    http://en.wikipedia.org/wiki/Veniamin_Grigorievich_Levichhttp://en.wikipedia.org/wiki/Veniamin_Grigorievich_Levich
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    Current Voltage Curve at a RDE

    It is important to remember that in order to determine the

    diffusion current and the mass transfer coefficient usingvolatmmetry, excess inert supporting electrolyte must be

    present to eliminate the migration current

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    Levich Equation The Levich Equation is written as:

    where

    iL is the Levich current

    n is the number ofelectrons transferred in the half reaction

    Fis the Faraday constant A is the electrode area

    D is the diffusion coefficient (see Fick's law of diffusion)

    wis the angular rotation rate of the electrode

    vis the kinematic viscosity Cis the analyte concentration

    While the Levich equation suffices for many purposes,improved forms based on derivations utilising more terms inthe velocity expression are available.[1][2]

    http://en.wikipedia.org/wiki/Electronshttp://en.wikipedia.org/wiki/Half_reactionhttp://en.wikipedia.org/wiki/Faraday_constanthttp://en.wikipedia.org/wiki/Fick's_law_of_diffusionhttp://en.wikipedia.org/wiki/Kinematic_viscosityhttp://en.wikipedia.org/wiki/Analytehttp://calctool.org/CALC/chem/electrochem/levichhttp://calctool.org/CALC/chem/electrochem/levichhttp://en.wikipedia.org/wiki/Analytehttp://en.wikipedia.org/wiki/Kinematic_viscosityhttp://en.wikipedia.org/wiki/Fick's_law_of_diffusionhttp://en.wikipedia.org/wiki/Faraday_constanthttp://en.wikipedia.org/wiki/Half_reactionhttp://en.wikipedia.org/wiki/Electrons
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    Rotating Disc Electrode

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    Levich Equation

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    Levich Equation

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    Levich Equation It is important to note that the layer of solution immediately

    adjacent to the surface of the electrode behaves as if it werestuck to the electrode. While the bulk of the solution is being

    stirred vigorously by the rotating electrode, this thin layer of

    solution manages to cling to the surface of the electrode and

    appears (from the perspective of the rotating electrode) to bemotionless.

    This layer is called the stagnant layer in order to distinguish it

    from the remaining bulk of the solution. The act of rotation

    drags material to the electrode surface where it can react.Providing the rotation speed is kept within the limits that

    laminar flow is maintained then the mass transport equation is

    given by the Levich equation.

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    Levich Equation RDE

    The Levich equation takes into account both the rate of

    diffusion across the stagnant layer and the complex solution

    flow pattern. In particular, the Levich equation gives the

    height of the sigmoidal wave observed in rotated disk

    voltammetry. The sigmoid wave height is often called the

    Levich current, iL, and it is directly proportional to the analyteconcentration, C. The Levich equation is written as:

    iL = (0.620) n F A D2/3 w1/2 v1/6 C

    where w is the angular rotation rate of the electrode

    (radians/sec) and v is the kinematic viscosity of the solution(cm2/sec). The kinematic viscosity is the ratio of the solution's

    viscosity to its density.

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    Current Voltage Curve at a RDE

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    Ilimiting vs (electrode rotational velocity)

    Le ich Eq ation RDE

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    Levich Equation - RDE

    The linear relationship between Levich current and the squareroot of the rotation rate is obvious from the Levich plot. A

    linear least squares fit of the data produces an equation forthe best straight line passing through the data. The specificexperiment shown, the electrode area, A, was 0.1963 cm2, theanalyte concentration, C, was 2.55x106 mol/cm3, and thesolution had a kinematic viscosity, v, equal to 0.00916cm2/sec. After careful substitution and unit analysis, you cansolve for the diffusion coefficient, D, and obtain a value equalto 4.75x106 cm2/s. This result is a little low, probably due tothe poor shape of the sigmoidal signal observed in thisparticular experiment.

    The kinematic viscosity is the ratio of the absolute viscosity of

    a solution to its density. Absolute viscosity is measured inpoises (1 poise = gram cm1 sec1). Kinematic viscosity ismeasured in stokes (1 stoke = cm2 sec1). Extensive tables ofsolution viscosity and more information about viscosity unitscan be found in the CRC Handbook of Chemistry and Physics.

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    Cyclic Voltammetry

    Cyclic Voltammetry is carried out at a stationary

    electrode.

    This normally involves the use of an inert disc

    electrode made from platinum, gold or glassy carbon.

    Nickel has also been used.

    The potential is continuously changed as a linear

    function of time. The rate of change of potential with

    time is referred to as the scan rate (v). Compared to a

    RDE the scan rates in cyclic voltammetry are usuallymuch higher, typically 50 mV s-1

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    Cyclic Voltammetry

    Cyclic voltammetry, in which the direction of the

    potential is reversed at the end of the first scan. Thus,

    the waveform is usually of the form of an isosceles

    triangle.

    The advantage using a stationary electrode is that theproduct of the electron transfer reaction that occurred in

    the forward scan can be probed again in the reverse

    scan.

    CV is a powerful tool for the determination of formalredox potentials, detection of chemical reactions that

    precede or follow the electrochemical reaction and

    evaluation of electron transfer kinetics.

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    Cyclic Voltammetry

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    Cyclic Voltammetry

    For a reversible

    process

    Epc Epa = 0.059V/n

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    The Randles-Sevcik equation Reversible systems

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    The Randles-Sevcik equation Reversible systems

    n = the number of electrons in the redox reaction

    v= the scan rate in V s-1 F = the Faradays constant 96,485 coulombs mole-1

    A = the electrode area cm2

    R = the gas constant 8.314 J mole

    -1

    K

    -1

    T= the temperature K

    D = the analyte diffusion coefficient cm2 s-1

    21

    4463.0 RTnFvDnFACip ACDvnip 212123510687.2

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    The Randles-Sevcik equation Reversible systems

    As expected a plot of peak height vs the square root of the scan rate

    produces a linear plot, in which the diffusion coefficient can be obtained

    from the slope of the plot.

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    Cyclic Voltammetry

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    Cyclic Voltammetry

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    Cyclic Voltammetry

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    Cyclic Voltammetry Stationary Electrode

    Peak positions are related to formal potential of redox

    process

    E0 = (Epa + Epc ) /2

    Separation of peaks for a reversible couple is 0.059/n volts

    A one electron fast electron transfer reaction thus gives

    59mV separation

    Peak potentials are then independent of scan rate

    Half-peak potential Ep/2 = E1/2 0.028/n

    Sign is + for a reduction

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    Cyclic Voltammetry Stationary Electrode

    The shape of the voltammogram depends on the transfer

    coefficient

    When deviates from 0.5 the voltammograms become

    asymmetric -cathodic peak sharper as expected from Butler

    Volmer eqn.

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    Web Sites

    http://calctool.org/CALC/chem/electrochem/l

    evich

    http://www.calctool.org/CALC/chem/electroc

    hem/cv1

    T f l E i

    http://calctool.org/CALC/chem/electrochem/levichhttp://calctool.org/CALC/chem/electrochem/levichhttp://www.calctool.org/CALC/chem/electrochem/cv1http://www.calctool.org/CALC/chem/electrochem/cv1http://www.calctool.org/CALC/chem/electrochem/cv1http://www.calctool.org/CALC/chem/electrochem/cv1http://calctool.org/CALC/chem/electrochem/levichhttp://calctool.org/CALC/chem/electrochem/levich
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    Tafel Equation

    The Tafel slope is an intensive parameter and does not

    depend on the electrode surface area.

    i0 is and extensive parameter and is influenced by the

    electrode surface area and the kinetics or speed of the

    reaction.

    Notice that the Tafel slope is restricted to the number of

    electrons, n, involved in the charge transfer controlled

    reaction and the so called symmetry factor, .

    n is often = 1 and although the symmetry factor can varybetween 0 and 1 it is normally close to 0.5.

    This means that the Tafel slope should be close to 120

    mV if n = 1 and 60 mV if n = 2.

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    Tafel Equation

    We can write:

    ii

    nF

    RTb

    iibiinF

    RT

    log303.2ln

    slopeTafelthe303.2

    where

    lnorln 00

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    Evans Diagrams

    i

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    Evans Diagrams

    E Di

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    Evans Diagrams