Literature DB >> 17256152

A phenomenological model to represent the kinetics of growth by Corynebacterium glutamicum for lysine production.

Kalyan Gayen1, K V Venkatesh.   

Abstract

Corynebacterium glutamicum is commonly used for lysine production. In the last decade, several metabolic engineering approaches have been successfully applied to C. glutamicum. However, only few studies have been focused on the kinetics of growth and lysine production. Here, we present a phenomenological model that captures the growth and lysine production during different phases of fermentation at various initial dextrose concentrations. The model invokes control coefficients to capture the dynamics of lysine and trehalose synthesis. The analysis indicated that maximum lysine productivity can be obtained using 72 g/L of initial dextrose concentration in the media, while growth was optimum at 27 g/L of dextrose concentration. The predictive capability was demonstrated through a two-stage fermentation strategy to enhance the productivity of lysine by 1.5 times of the maximum obtained in the batch fermentation. Two-stage fermentation indicated that the kinetic model could be further extended to predict the optimal feeding strategy for fed-batch fermentation.

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Year:  2007        PMID: 17256152     DOI: 10.1007/s10295-007-0205-9

Source DB:  PubMed          Journal:  J Ind Microbiol Biotechnol        ISSN: 1367-5435            Impact factor:   4.258


  16 in total

1.  Kinetic models for the growth of Escherichia coli with mixtures of sugars under carbon-limited conditions.

Authors:  U Lendenmann; T Egli
Journal:  Biotechnol Bioeng       Date:  1998-07-05       Impact factor: 4.530

2.  An optimal strategy to model microbial growth in a multiple substrate environment.

Authors:  K V Venkatesh; P Doshi; R Rengaswamy
Journal:  Biotechnol Bioeng       Date:  1997-12-20       Impact factor: 4.530

3.  Microbial growth on substitutable substrates: characterizing the consumer-resource relationship.

Authors:  R Ramakrishna; D Ramkrishna; A E Konopka
Journal:  Biotechnol Bioeng       Date:  1997-04-05       Impact factor: 4.530

4.  Structured kinetic model to represent the utilization of multiple substrates in complex media during rifamycin B fermentation.

Authors:  Prashant M Bapat; Sharad Bhartiya; K V Venkatesh; Pramod P Wangikar
Journal:  Biotechnol Bioeng       Date:  2006-03-05       Impact factor: 4.530

5.  Influence of glucose, fructose and sucrose as carbon sources on kinetics and stoichiometry of lysine production by Corynebacterium glutamicum.

Authors:  P Kiefer; E Heinzle; C Wittmann
Journal:  J Ind Microbiol Biotechnol       Date:  2002-06       Impact factor: 3.346

6.  General organization of the genes specifically involved in the diaminopimelate-lysine biosynthetic pathway of Corynebacterium glutamicum.

Authors:  P Yeh; A M Sicard; A J Sinskey
Journal:  Mol Gen Genet       Date:  1988-04

Review 7.  Network rigidity and metabolic engineering in metabolite overproduction.

Authors:  G Stephanopoulos; J J Vallino
Journal:  Science       Date:  1991-06-21       Impact factor: 47.728

8.  Metabolic flux distributions in Corynebacterium glutamicum during growth and lysine overproduction.

Authors:  J J Vallino; G Stephanopoulos
Journal:  Biotechnol Bioeng       Date:  1993-03-15       Impact factor: 4.530

Review 9.  Biotechnological manufacture of lysine.

Authors:  Walter Pfefferle; Bettina Möckel; Brigitte Bathe; Achim Marx
Journal:  Adv Biochem Eng Biotechnol       Date:  2003       Impact factor: 2.635

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