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bioreactor studies of heterologous protein production by ...

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detennined in the cunent study, the model was able to simulate the fiaction <strong>of</strong> plasmid-<br />

bearing cells <strong>of</strong> the cited nxombinant strain. Coppella and Dhurjati also developed an<br />

excenent smcnired model to descnbe the recombinant yeast (Coppeb and Dhq0ati,<br />

1990). But their model required 43 equatioas and 48 parameters and some parameters<br />

were dificuit to estimate. Its complexity poses a number <strong>of</strong> diEicuIties for its practical use<br />

(e.g. parameter estimations). In con- the present model requins 15 equations and 18<br />

experimentaliy accessible parameters. It is more realistic and useful for industriai<br />

applications.<br />

In order to further test the proposed mode4 another set <strong>of</strong> experimental data on<br />

die growth <strong>of</strong> recombinant S. cerevisiue SEY2102/pRB58 wen obtained h m Parker and<br />

Seo (1992). The host saain SEY 2102 contained the plasmid pBR58. which encodes for<br />

intraceilular invertase. The dynamics <strong>of</strong> ce1 growth. glucose consumption and ethanol<br />

metabohm wen sirnuiated <strong>by</strong> the modeL Dw to inadequate data, the simulation for<br />

invertase <strong>production</strong> could not be presented. Figure 5.4 shows a remarkable agreement<br />

benHeen the model simulations and the reported dam In executing the model. the same<br />

parameter values hted in Table I were used except the value <strong>of</strong> p~, iJ,, and th, which were<br />

set to 0.10 If' and 1.5 h respectively to match the observed values. Thus. the general<br />

applicability <strong>of</strong> the present model was furcher confîmed.

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