Eg Reactor Design

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  • 7/27/2019 Eg Reactor Design

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    EG REACTOR DESIGN

    As we are using %90 excess of water, reaction will be Pseudo First Order reaction.

    n=1CA=Cao(1-XA)

    k=0,23 min-1

    Conversion =0,80

    Total molar flow rate in = Fti= 7111,5 kmol/h

    EO=646,5 kmol/h

    Water= 6465,5kmol/h

    E (Activation Energy) = 110 kJ/mole

    As we know the formula for the volume of the reactor

    By integration,

    A

    AA

    A

    A

    X

    XkC

    dXFV

    0)1(

    /0

    0

    )1ln(

    1

    / 00 A

    A

    A XkC

    FV

    We need 0AC and 0AF ;

    Total Molar Flow Rate In= 0AF = 7111,5 kmol/h

    0AC = kmoles of Ethylene Oxide/Volume of the mixture

    kmoles of Ethylene Oxide = 646,5 kmol/h

    Now we need Volume of the mixture;

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    Volume of the mixture = Total weight of the mixture/Density of the mixture

    Total weight of the mixture = 144845,91 kg/h

    Now Density of the mixture;

    Density of Water ( OH2 ) =]5340.2

    )4713.6

    4681(1[

    01

    00

    01

    02

    )4870.2(

    3910.4

    E

    EE

    E

    By solving the above Equation

    Density of Water =

    722.1

    2487.0

    391.4=

    091.0

    391.4=48.25 kmole/m

    3

    =48.25kmole/ m3

    * 18 kg/kmole

    Density of Water ( OH2 ) =868.5 kg/ m3

    Density of Ethylene Oxide ( EO) =

    ])15.469468

    1(1[2696.0

    26024.0

    836.1

    By solving the above Equation

    = 19775.126024.0

    836.1

    =

    199.0

    836.1

    = 9.226 kmole/m3

    = 9.226 kmole/m3

    * 44 kg/kmole

    Density of Ethylene Oxide ( EO) = 405.9 kg/ m3

    Now

    Density of the mixture =

    5.868

    91,144845

    1163709.405

    91,144845

    91,28475

    = (0.09*405.9) + (0.91*868.5)

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    = 826,866 kg/ m3

    By using Equation for Volume of the mixture, so

    Volume of the mixture =

    = 175,175 m3

    And

    0AC == 3.654 kmol/m

    3

    Now

    )1ln(0

    0

    A

    A

    X

    kC

    FAV

    By putting the values, we get

    Volume of PFR = 20,65 m3

    Residence Time:

    / oV v

    = 20,65/175,175

    = 7,07 min.

    Length of Pipe:

    Volume of reactor = V = /4 (D2L)

    L/D = 200 (P.F.R)

    L = 200 * D

    V = 50 D3

    D = (V/50 )1/3

    D = (20,65/50* )1/3

    D = 0.508 m

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    L = 200 * 0.52 = 101,7 m

    Selection of Pipe:

    Nominal Pipe Size = 2 Schedule No. 80

    Required Flow Area for Plug Flow = /4 (0.508)2

    = 0.203 m2

    Flow Area of 2, Schedule No. 80

    I.D = 1.939 in=0,04925 m

    O.D = 2,38 in = 0,065 m

    Flow Area of one tube = 1.9048 * 10-3

    m2

    No. of pipes required/pass = 0.203/1.9048 * 10-3

    = 107 pipes

    Assume 8 passes:-

    Length of each pipe = 107/8

    = 13,37 m

    Length of pipe = 101,7/8 =12,7 m

    Total no. of pipes = 107 * 8

    = 856 pipes

    Thus Total pipe passes = 8