Literature DB >> 18592595

A general model for aerobic yeast growth: batch growth.

J P Barford1.   

Abstract

A general model for aerobic yeast growth in batch culture is presented. It is based on the concept that the aerobic metabolism of all yeasts is determined by the relative sizes of the transport rate of sugar into the cell and the transport rate of respiratory intermediates into the mitochondrion. If the rate of sugar uptake rate exceeds the rate of transport of respiratory intermediates into the mitochondrion (as in Saccharomyces cerevisiae, S. uvarum, and S. pombe), the metabolism exhibits the features of ethanol excretion and limited specific oxygen uptake rate. If the rate of transport of respiratory intermediates into the mitochondrion is of the same order as the transport of sugar into the cell (as in Candida utilis), the metabolism is characterized by little or no ethanol excretion and a much higher specific oxygen uptake rate. Batch data from an extensive range of yeast and carbon sources is used to illustrate the use of this model. The ability of this model to fit such an extensive range of experimental data suggests that it can be used as a generalized model for aerobic yeast growth.

Entities:  

Year:  1990        PMID: 18592595     DOI: 10.1002/bit.260350908

Source DB:  PubMed          Journal:  Biotechnol Bioeng        ISSN: 0006-3592            Impact factor:   4.530


  4 in total

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2.  Estimation of the energetic biomass yield and efficiency of oxidative phosphorylation in cell-recycle cultures of Schizosaccharomyces pombe.

Authors:  J Humberto de Queiroz; J L Uribelarrea; A Pareilleux
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3.  Altering the ribosomal subunit ratio in yeast maximizes recombinant protein yield.

Authors:  Nicklas Bonander; Richard Aj Darby; Ljuban Grgic; Nagamani Bora; Jikai Wen; Saverio Brogna; David R Poyner; Michael Aa O'Neill; Roslyn M Bill
Journal:  Microb Cell Fact       Date:  2009-01-29       Impact factor: 5.328

4.  Enzyme-constrained models predict the dynamics of Saccharomyces cerevisiae growth in continuous, batch and fed-batch bioreactors.

Authors:  Sara Moreno-Paz; Joep Schmitz; Vitor A P Martins Dos Santos; Maria Suarez-Diez
Journal:  Microb Biotechnol       Date:  2022-01-20       Impact factor: 6.575

  4 in total

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