Reactor Design for Cell Groth

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    07 Oct 2011 Prof. R. Shanthini 1

    Cellular kinetics and associated reactor design:

    Reactor Design for Cell Growth

    CP504 ecture 7

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    Cell Growth Kinetics

    r! " # C! $41%

    &here

    # : s'ecific gro&th rate $'er ti(e%

    C! : cell concentration $dr) cell &eight 'er unit *olu(e%

    +sing the 'o'ulation gro&th (odel, &e could &rite the cell

    gro&th rate $r!% as

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    for *olu(e of the reacting (i/ture at ti(e t

    C!for concentration of the cells in at ti(e t

    $r!% for cell gro&th rate in at ti(e t

    ass alance for the cell:

    0 $r!% " 0 d$C!% 3 dt

    &hich for a atch reactor &ith constant *olu(e

    reacting (i/ture gi*es

    $42%

    Batch Fermenter

    dC! 3 dt " r!

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    Co(ining $41% and $42%, &e get

    dC!" # C!

    dt$4-%

    Batch Fermenter

    f # is a constant then integrating $4-% gi*es,

    C! " C!0e/'#$t6t0% $44%

    &here C!" C!0&hen t " t0.

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    Cell Growth Kinetics

    &here #(a/and 8Sare kno&n as the onod kinetic 'ara(eters.

    ostl), ho&e*er, # is not a constant &ith ti(e. t de'ends on

    CS

    , the sustrate concentration.

    9he (ost co((onl) used (odel for # is gi*en ) the onod

    (odel:

    Monod Modelis an o*er si('lification of the co('licated

    (echanis( of cell gro&th.

    o&e*er, it ade;uatel) descries the kinetics &hen the

    concentrations of inhiitors to cell gro&th are lo&.

    # "8

    S C

    S

    #(CS $45%

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    07 Oct 2011 Prof. R. Shanthini ut &e don?t kno& $6rS%.

    9herefore otain an e/'ression for $6rS% as sho&n in the ne/t

    slide.

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    for *olu(e of the reacting (i/ture at ti(e t

    CSfor concentration of the Cells in at ti(e t

    $rS% for sustrate utiliation rate in at ti(e t

    ass alance for sustrate:

    0 " 0 $6rS% d$CS% 3 dt

    &hich for a atch reactor &ith constant *olu(e

    reacting (i/ture gi*es

    $4B%dCS 3 dt " 6$6rS%

    Batch Fermenter

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    $4B%dCS 3 dt " 6$6rS%

    @!3S" 6 rS

    r!$47%

    $42%dC! 3 dt " r!

    Co(ining the ao*e e;uations, &e get

    dC! 3 dCS" 6@!3S

    &hich u'on integration gi*es

    (CX CX!" # $X%& (C&! C&" $4D%

    Batch Fermenter

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    Sustituting CSfro( $4D% in $47% and integrating, &e get

    #( $t 6 t0% "8S@!3S

    C!0 CS0@!3S

    1 lnC!0

    C!

    8S@!3S

    C!0 CS0@!3S

    lnCS

    CS0$50%

    &here

    $C! C!0% " @!3S $CS0 CS% $4D%

    Batch Fermenter

    ( )( )

    ))( (

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    'ercise ):

    9he gro&th rate of E. colie e/'ressed ) onod kinetics

    &ith #(" 0.D-5 hr61and 8S" 0.71 g3.

    Essu(e that @!3Sis 0.< g dr) cells 'er g sustrate.

    C!0is 1 g3 and CS0" 10 g3 &hen the cells start to gro&

    e/'onentiall) $i.e., at t " 0%.

    sho& ho& C!, CS, and dC!3dt change &ith res'ect to ti(e.

    Batch Fermenter

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    CSis *aried fro( 10 g3 to 0.

    ( )( )0.D-5t "

    0.71 / 0.CX= C&

    Continuous Stirred 9ank Ler(enter $CS9L% at stead)6state

    ass alance for cells o*er :

    LC!i r! " LC! $5-%

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    =;uation $5-% gi*es

    L"

    C!6 C!i

    r!$54%

    Continuous Stirred 9ank Ler(enter $CS9L% at stead)6state

    ntroducing Nilution Rate Nas

    " $55%L

    N "

    1

    M

    in $54%, &e get

    1

    N"

    C!6 C!i

    r!$5

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    Since r!" # C!, $5

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    CS " $

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    FCXi= C&i

    F

    CX= C&

    >CX= C&

    ass alance for sustrate o*er :

    LCSi" LCS $6rS%

    Continuous Stirred 9ank Ler(enter $CS9L% at stead)6state

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    &hich is rearranged to gi*e

    $6rS% " N $CSi6 CS% $

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