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  • 11
    ISSN: 0138-4988
    Keywords: Life Sciences ; Life Sciences (general)
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: The ethanol-inhibitory behaviour of the yeast Saccharomyces cerevisiae Sc 5 was found to be characterized by a continual-linear relation between the specific ethanol formation rate and the ethanol concentration. Therefore the simple equation \documentclass{article}\pagestyle{empty}\begin{document}$$v = v_0 - a \cdot P$$\end{document} could be applied for it.It is shown that this model is correct only then, if all of the process parameters are in their optimum.Out of the optimum temperature range the characteristics of the function ν = f(P) change in such a way that in regard to the ethanol concentration P twc linear relations exist for each suboptimum temperature: \documentclass{article}\pagestyle{empty}\begin{document}$$ \begin{array}{*{20}c} {v_T = v'_{0T} - a_0 \cdot e^{nT} \cdot P,} & {{\rm for}} & {P 〈 P_T } & {{\rm and}} \\\end{array} $$\end{document} \documentclass{article}\pagestyle{empty}\begin{document}$$ \begin{array}{*{20}c} {v_T = v_0 - a \cdot P,} & {{\rm for}} & {P 〉 P_T ,} \\\end{array} $$\end{document} and a non-linear equation is current for each superoptimum temperature: \documentclass{article}\pagestyle{empty}\begin{document}$$ v_T = v'_{0T} - a_0 ^\prime \cdot e^{mT} \cdot P^{b_T } , $$\end{document} where bT is also a function of the temperature and always less than 1.Taking as a basis these equations the specific ethanol formation rate of the used strain can be calculated for the whole biokinetic P/T-sphere of ethanol production.
    Additional Material: 6 Ill.
    Type of Medium: Electronic Resource
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  • 12
    Electronic Resource
    Electronic Resource
    Berlin : Wiley-Blackwell
    Acta Biotechnologica 9 (1989), S. 123-129 
    ISSN: 0138-4988
    Keywords: Life Sciences ; Life Sciences (general)
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: The continuous ethanol production by free and Ca-alginate-entrapped cells of the yeast Saccharomyces cer. IBT H 191 was investigated in a membrane reactor and in a CSTR, respectively. An empiric productivity model for free-cell fermentation was found to be valid for immobilized cells if no external diffusion resistance existed within the reactor. In such a case the fermentative power of the immobilized cells was identical with this one of the free cells. A change of the ethanol-tolerance behaviour of the cells as a result of the cell-immobilization did not occur.
    Additional Material: 3 Tab.
    Type of Medium: Electronic Resource
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