Modelling of an industrial biotransformation process for tryptophan production

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Original languageEnglish
Pages (from-to)189-193
Number of pages5
JournalIFAC Proceedings Volumes (IFAC-PapersOnline)
Volume37
Issue number3
Publication statusPublished - 2004
Event9th IFAC International Symposium on Computer Applications in Biotechnology, CAB 2004 - Nancy, France
Duration: 28 Mar 200431 Mar 2004

Abstract

For an industrial biotransformation process a simple mathematical model has been developed. Inuring the process indole and serine is converted to tryptophan using the enzyme tryptophan synthase, which is supplied in E. coli cells. The tryptophan production has been described by a first order kinetic with respect to serine and the relative cell concentration as well as zero order kinetics with respect to indole. The 10.000 L reactor, in which the production is performed, is described as an ideal stirred tank reactor. The activity of the cell suspension, i. e. the activity of the tryptophan synthase, which was considered in one of the model parameter could be determined from fluorescence measurements (fluorescence intensity at 350 nm excitation and 470 nm emission wavelength) using a linear regression model. The model prediction corresponds very well with off-line measurement.

Keywords

    Automation, Biotechnology, Fluorescence, Mathematical model, Prediction, Tryptophan production

ASJC Scopus subject areas

Cite this

Modelling of an industrial biotransformation process for tryptophan production. / Solle, Dörte; Faurie, Robert; Breccia, Javier et al.
In: IFAC Proceedings Volumes (IFAC-PapersOnline), Vol. 37, No. 3, 2004, p. 189-193.

Research output: Contribution to journalConference articleResearchpeer review

Solle, D, Faurie, R, Breccia, J, Scheper, T & Hitzmann, B 2004, 'Modelling of an industrial biotransformation process for tryptophan production', IFAC Proceedings Volumes (IFAC-PapersOnline), vol. 37, no. 3, pp. 189-193. https://doi.org/10.1016/S1474-6670(17)32581-8
Solle, D., Faurie, R., Breccia, J., Scheper, T., & Hitzmann, B. (2004). Modelling of an industrial biotransformation process for tryptophan production. IFAC Proceedings Volumes (IFAC-PapersOnline), 37(3), 189-193. https://doi.org/10.1016/S1474-6670(17)32581-8
Solle D, Faurie R, Breccia J, Scheper T, Hitzmann B. Modelling of an industrial biotransformation process for tryptophan production. IFAC Proceedings Volumes (IFAC-PapersOnline). 2004;37(3):189-193. doi: 10.1016/S1474-6670(17)32581-8
Solle, Dörte ; Faurie, Robert ; Breccia, Javier et al. / Modelling of an industrial biotransformation process for tryptophan production. In: IFAC Proceedings Volumes (IFAC-PapersOnline). 2004 ; Vol. 37, No. 3. pp. 189-193.
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abstract = "For an industrial biotransformation process a simple mathematical model has been developed. Inuring the process indole and serine is converted to tryptophan using the enzyme tryptophan synthase, which is supplied in E. coli cells. The tryptophan production has been described by a first order kinetic with respect to serine and the relative cell concentration as well as zero order kinetics with respect to indole. The 10.000 L reactor, in which the production is performed, is described as an ideal stirred tank reactor. The activity of the cell suspension, i. e. the activity of the tryptophan synthase, which was considered in one of the model parameter could be determined from fluorescence measurements (fluorescence intensity at 350 nm excitation and 470 nm emission wavelength) using a linear regression model. The model prediction corresponds very well with off-line measurement.",
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AU - Solle, Dörte

AU - Faurie, Robert

AU - Breccia, Javier

AU - Scheper, Thomas

AU - Hitzmann, Bernd

PY - 2004

Y1 - 2004

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AB - For an industrial biotransformation process a simple mathematical model has been developed. Inuring the process indole and serine is converted to tryptophan using the enzyme tryptophan synthase, which is supplied in E. coli cells. The tryptophan production has been described by a first order kinetic with respect to serine and the relative cell concentration as well as zero order kinetics with respect to indole. The 10.000 L reactor, in which the production is performed, is described as an ideal stirred tank reactor. The activity of the cell suspension, i. e. the activity of the tryptophan synthase, which was considered in one of the model parameter could be determined from fluorescence measurements (fluorescence intensity at 350 nm excitation and 470 nm emission wavelength) using a linear regression model. The model prediction corresponds very well with off-line measurement.

KW - Automation

KW - Biotechnology

KW - Fluorescence

KW - Mathematical model

KW - Prediction

KW - Tryptophan production

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