l4_molecular diffusion in liquids

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    Molecular diffusion in Liquids

    Diffusion coefficient in liquids is slower than ingases (105 times lower).

    The flux in liquid is lower around 100 times

    than in gases. DABis composition dependent and it is slower

    than in the gases.

    1

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    Equations for diffusion in liquids

    2

    A A A AB A BdC C

    N D N N dz C

    Equimolar counter diffusion (NA = - NB )

    1 2

    2 1

    AB A A

    A

    D C C N

    z z

    1 2

    2 1

    AB avg A A

    A

    D C x x

    N z z

    1 21 2

    2

    M M

    avgC

    DAB is a function of composition, therefore it

    must be calculated based on the average

    values between point 1 and 2

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    Equations for diffusion in liquids

    3

    Diffusion of solute (A) through stagnant solvent (B) (NB

    = 0)

    1 2

    2 1

    A B avg A AA

    BLM

    D C x xN

    z z x

    2

    1

    2 1

    ln( )BB

    B BBLM x

    x

    x xx

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    Example

    An ethanol (A)-water (B) solution in the form ofa stagnant film 2.0 mm thick at 293 K is incontact at one surface with an organic solvent inwhich ethanol is soluble and water is insoluble.

    Hence, NB =0. At point 1 the concentration ofenthanol is 16.8 wt% and the solution density is1 = 972.8kg/m

    3. At point 2 the concentration ofethanol is 6.8 wt% and

    2= 988.1 kg/m3 . The

    diffusivity of ethanol is 0.740e-9 m2/s. Calculatethe steady-state flux NA.

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    Solution

    5

    MA

    = 46.05, MB

    =18

    16.846.05

    116.8 83.2

    46.05 18

    0.073Ax

    20.0277Ax

    xB1 = 0.9268, xB2 = 0.9723

    116.8 83.2

    46.05 18

    10020.07M

    218.75M

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    Solution cont.

    6

    972.8 988.120.07 18.75

    50.62

    avgC Kg mol/m3

    xBLM = 0.949

    90.740 10 50.6 0.0732 0.0277

    2 / 1000 0.949AN

    NA = 8.99e-7 kg mol/s. m2

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    Liquid Diffusivity, DAB

    DAB= f(T,P,C).

    Effect of pressure is insignificant compared totemperature and concentration.

    DAB DBA

    Several eqns to estimate the liquid diffusivityare available, however not all of them can give

    an accurate prediction. Successful equations are developed for dilute

    mixtures.

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    Equations for DAB

    8

    DAB

    for dilute solution 1. Wilke and Chang (1955)

    1

    213

    0.6

    1.17 10 B BAB

    A

    M TD

    V

    ABD Diffusion coefficient in dilute solution, m

    2/s

    MB = Molecular weight of the solvent

    VA = Molar volume of solute at normal boiling point, m3 /kgmol

    B = Association factor for solventSolvent

    Non-polar 1

    Water 2.6

    Methanol 1.9

    Ethanol 1.5

    = viscosity of solution, cP

    Error is within 11% when water is

    the solvent, and 27% for organic

    solvent.

    Error can reach up to 200% when

    water is the solvent

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    Equations for DAB

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    DAB

    for concentrated solution

    1. Vignes (1966)

    ln

    1ln

    B Ax x A A B A B BA

    A

    D D Dx

    A = Activity coefficient of solute

    2. Leffler and Cullinan (1970)

    ln

    1

    ln

    B Ax x A AB mix AB B BA A

    A

    D D D

    x