Multiphase Bioreactor Design

(avery) #1
Alcoholic fermentation of glucose by Ca-alginate immobilised
Saccharomyces cerevisiae

Alcoholic fermentation is a process often affected by the presence of the product, which
causes a progressive decrease in the production rate until a threshold value is reached at


Table 11.2 Kinetic parameters of the enzymatic


hydrolysis of starch operating in packed-bed


bioreactor with and without pulsation


Packed-bed reactor Without pulsation With pulsation


S (gL−^1 ) Vmax KM Vmax KM


50 0.099 12.44 0.110 12.42


100 0.097 13.02 0.123 12.50


150 0.102 13.36 0.144 12.53


Figure 11.5 Effects of pulsation on


enzymatic hydrolysis of starch in


pulsed and non-pulsed packed-bed


bioreactors for different substrate


concentrations at a hydraulic retention


time of 1 h.


which it stops. Accordingly, for this process, a hydraulic behaviour such as plug flow is
desirable.


Pulsing bioreactors 339
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