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bioreactor studies of heterologous protein production by ...

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The finai giucoamyiase concentration in the ALR (153 unitsk) was much higher<br />

than that in ihe STR (66 unitSn,) although the nnal ceii concentrations in both <strong>bioreactor</strong>s<br />

were nearly the same (Fignre 4.3). This result may be related to the difference in the<br />

specifc growth rate in the suxind growth phase. It appears that the recombinant <strong>protein</strong><br />

yield decreased with increasing specific gmwth rate <strong>of</strong> the recombinant yeast The<br />

relatiowhip between the recombinant <strong>protein</strong> yield and specitic growth rate will be further<br />

discussed in the next section.<br />

4.2.3. Effect <strong>of</strong> Specific Growth Rate on Recombinant Protein Yield<br />

Figures 4.3 and 4.4 demonstrated that dissolved oxygen tension in the <strong>bioreactor</strong> affects<br />

the specific growth rate, and the recombinant <strong>protein</strong> <strong>production</strong> was directiy related to<br />

the specific growth rate. In order to Mer test this phenornenon. a batch culture<br />

fementation was performed in the STR <strong>bioreactor</strong> ushg lower aeration rate (0.4 VVM).<br />

Due to decreased dissolved oxygen in the <strong>bioreactor</strong>. the batch fermentation was<br />

prolonged but the final glucoamylase concentration increased h m 61 to 91 uniW. Thus,<br />

the enhanced combinant <strong>protein</strong> yield due to die slower growth rare was shown again.<br />

The specific growth rates for both exponential phases were determined hm the<br />

semilogacithmic plots <strong>of</strong> celi concentration versus the as shown in Figure 4.5. The<br />

giucoamylase yields were evaluated from hear regression <strong>of</strong> glucoamylase concentrations<br />

to c d concentrations as show in Figure 4.6. The parameter estimates are iisted in Table<br />

4.1. Table 4.1 shows that the speciîïc pwth rates in the fint growth phase (on glucose)

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