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7/23/2019 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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07 Oct 2011 Prof. R. Shanthini 2
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
7/23/2019 Reactor Design for Cell Groth
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07 Oct 2011 Prof. R. Shanthini -
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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07 Oct 2011 Prof. R. Shanthini 4
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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07 Oct 2011 Prof. R. Shanthini 5
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%
7/23/2019 Reactor Design for Cell Groth
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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.
7/23/2019 Reactor Design for Cell Groth
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07 Oct 2011 Prof. R. Shanthini B
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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07 Oct 2011 Prof. R. Shanthini D
$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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07 Oct 2011 Prof. R. Shanthini 10
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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07 Oct 2011 Prof. R. Shanthini 11
'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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07 Oct 2011 Prof. R. Shanthini 12
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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07 Oct 2011 Prof. R. Shanthini 21
=;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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07 Oct 2011 Prof. R. Shanthini 22
Since r!" # C!, $5
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07 Oct 2011 Prof. R. Shanthini 2-
CS " $
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07 Oct 2011 Prof. R. Shanthini 24
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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07 Oct 2011 Prof. R. Shanthini 25
&hich is rearranged to gi*e
$6rS% " N $CSi6 CS% $
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07 Oct 2011 Prof. R. Shanthini 2