diffusion problem

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  • 8/18/2019 Diffusion problem

    1/4

    1. Calculate the rate of diusion of sugar through a stagnant lm of coee

    0.10 cm thick when the concentrations at 15% and 5%, respectively, on

    either side of the lm. ssume the diusivity of sugar through coee

    under the given conditions to !e 0."0 # 10$5 cm&s and the density of a

    10% solution is 1.01'( g&cc.

    )iven*

    +v 0."0 # 10$5 cm&s

    -10% wt solution 1.'( g&cc

    /euired*

    2olution* 3nicomponent

    +iusion

      xA 1=

    15

    342

    15

    342  +

    85

    18

    xA 1=0.00920

      xA 2=

    15

    342

    15

    342  +

    95

    18

    xA 2=0.00276

  • 8/18/2019 Diffusion problem

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      x10%=

    10

    342

    10

    342  +

    90

    18

    x10%

    =0.00581

     M 10=0.00581 (342g /mol)+(1−0.00581)(18 g /mol )

     M 10=¿ 1(.44 g&mol

    C  Ave=  ρ

    10

     M 10=

      1.0139g /cc19.8824 g/mol  

    C  Ave=0.0510mol /cc

     N  A=0.70 x 10

    −5 cm2

    s (0.0510molcc )0.10cm

      ln

    (1−0.00276

    1−0.00920 ) 

     N  A=2.3129 x10−8  mol

    cm2s≈2.3129 x10

    −7 kmol

    m2s

    . n rnold cell is used to measure the diusivity of acetone in air at 0C

    and 100 k6a pressure. t time 0, the liuid acetone surface is 1.10 cm

    from the top of the tu!e and after 4 hours of operation, the liuid surface

    drops to .05 cm. if the concentration of acetone in air that 7ows over the

    top of the tu!e is 8ero, what is the diusivity of acetone in air9 t 0C,

    the vapor pressure of acetone is k6a and density is "(0 kg&m'.

    )iven*

  • 8/18/2019 Diffusion problem

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    6acetone k6a

    - acetone "(0 kg&m'

    /euired* + acetone$air : 0C,

    100 k6a

    2olution*

     P(¿¿T − P A) L P A1− P A2

    ¿¿

    2 t f  ρm MW  ¿

     Dv=( z

    2

    2− z1

    2)( ρacetone)¿

     ρm=

     PT  RT  =

    100 kPa(   1atm101.325kPa )0.08205

     m3atm

    kmolK (20+273 ) K 

     ρm=0.0411kmol /m3

     P A1

    = P ° A x A=24kPa (1 )=24 kPa

     P A2

    =0kPa

  • 8/18/2019 Diffusion problem

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     P

     P P

    (¿¿T − P A2)−

     (¿ ¿T − P A1)

    ln

    ( PT − P A

    1

     PT − P A2 )

    =(100−0)−(100−24)

    ln

    (  100−0

    100−24 )

      =87.4518 kPa

    ¿(¿¿T − P A) L=¿

    ¿

     Dv=

    (0.02052−0.01102 )m2(790 kgm3 )2 (8h )(0.0411 kmolm3 )(58

      kg

    mol )(   24−0

    87.4518 )( 3600 s1h   )

     Dv=6.2737 x 10−6m

    2

    s