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(ranghg h m 1 to 7) on citric acid productivity was examined. They obsewed that the<br />

highest productivity was obtained at the height-to-diameter ratio <strong>of</strong> 3.<br />

Aïmost dl previous <strong>studies</strong> involve three-phase sluny airlift reactor with gel<br />

entrapped imrnob~ ceh. For hydrogel ixnmobilized ceiis, the dismption problem still<br />

exists in the airlift reactor. As discossed above, the use <strong>of</strong> s<strong>of</strong>t and highly porous nanual<br />

or synthetic materiais may ovmorne this. However, sluny three-phase airiift reacfors are<br />

not suitable with these materials due to iheir low density. Even after loading with<br />

biomass. they stül have a density equal to or less than that <strong>of</strong> the continuous liquid phase.<br />

Whde the particles firculating through the airiift reactor, they tend to block the<br />

downcomer if the particle loading inmases to certain levei, causing the instability <strong>of</strong><br />

reactor operation (prelUninary experiment restüt). Besides, liquid-solid mas mfer<br />

limitation may occur in the reactor due to low liquid-soiid slip velocity. Many <strong>of</strong> these<br />

<strong>studies</strong> were conducted on a srnail scale. and concemed mainly with the feasibility and<br />

fermentation kinetics rather than biopmess development and transport phenornena. Littie<br />

information is avaüable for airlift design, operation. and scale-up during actuai<br />

fermentation processes. Therefore, mnch work is ttrgently needed in these aspects.<br />

2.5. Modelling <strong>of</strong> Recombinant Yeast<br />

Interest ui modeliing <strong>of</strong> piasruid instability kinetics in recombinant ce& has increased with<br />

our better understanding <strong>of</strong> the mechanism <strong>of</strong> piasmid uistability. In nirn, such modehg<br />

can provide valuable info~mation about the natore <strong>of</strong> piasmid instability and give a greater

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