Design of Fermentation Processes
357
S
S
S
s
Figure 9.3. Productivity of a steady state stirred tank reactor.
A. Monod kinetics :
jumax =
0.5 h ',
Ks =
0.4 g I /1
.
sf = 2g
= 0.5 g L'1.
B. Substrate inhibition : As in A, and
K, =
0.25 g L‘\ i.e.
b =
8 in Eq (9.28).
C. Product inhibition (Eq (7.23)): As in A, and
SfYsp/pmax
= 2/3.
D. Maintenance (Eq (9.13),(9.14)): As in A, and
b -
0.2 in Eq (5 E9.2).
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