Modelling and simulation of the enzymatic hydrolysis of potato pulp by a complex enzyme mixture

Research output: Contribution to journalArticleResearchpeer review

Authors

  • J. Bader
  • K. H. Bellgardt
  • K. Schügerl

Research Organisations

View graph of relations

Details

Original languageEnglish
Pages (from-to)B13-B19
JournalThe Chemical Engineering Journal
Volume52
Issue number1
Publication statusPublished - Aug 1993

Abstract

The enzymatic hydrolysis of potato pulp by a cell-free culture filtrate of Trichoderma reesei Rut C30 was studied. On the basis of the experimental data a dynamic unstructured model using Michaelis-Menten kinetics was developed. This mathematical model describes the enzymatic hydrolysis in terms of the adsorption and desorption of enzymes on the solid substrate and with regard to competitive and uncompetitive inhibition. The model equations consist of a non-linear system of ordinary differential and algebraic equations. Parameter identification was done by dividing the model into submodels and fitting these to experimental data. The simulation results with the model correspond well with the experimental data. Thus the good agreement between simulated and measured process variables indicates that the model is suitable for description of the enzymatic hydrolysis. Computations for different operational conditions show the range of validity and performance of the model. Possibilities for improvements in yield and productivity could be deduced by model computations.

ASJC Scopus subject areas

Cite this

Modelling and simulation of the enzymatic hydrolysis of potato pulp by a complex enzyme mixture. / Bader, J.; Bellgardt, K. H.; Schügerl, K.
In: The Chemical Engineering Journal, Vol. 52, No. 1, 08.1993, p. B13-B19.

Research output: Contribution to journalArticleResearchpeer review

Bader J, Bellgardt KH, Schügerl K. Modelling and simulation of the enzymatic hydrolysis of potato pulp by a complex enzyme mixture. The Chemical Engineering Journal. 1993 Aug;52(1):B13-B19. doi: 10.1016/0300-9467(93)80045-P
Bader, J. ; Bellgardt, K. H. ; Schügerl, K. / Modelling and simulation of the enzymatic hydrolysis of potato pulp by a complex enzyme mixture. In: The Chemical Engineering Journal. 1993 ; Vol. 52, No. 1. pp. B13-B19.
Download
@article{932dbaa754614c27ba4fd10c3f58075f,
title = "Modelling and simulation of the enzymatic hydrolysis of potato pulp by a complex enzyme mixture",
abstract = "The enzymatic hydrolysis of potato pulp by a cell-free culture filtrate of Trichoderma reesei Rut C30 was studied. On the basis of the experimental data a dynamic unstructured model using Michaelis-Menten kinetics was developed. This mathematical model describes the enzymatic hydrolysis in terms of the adsorption and desorption of enzymes on the solid substrate and with regard to competitive and uncompetitive inhibition. The model equations consist of a non-linear system of ordinary differential and algebraic equations. Parameter identification was done by dividing the model into submodels and fitting these to experimental data. The simulation results with the model correspond well with the experimental data. Thus the good agreement between simulated and measured process variables indicates that the model is suitable for description of the enzymatic hydrolysis. Computations for different operational conditions show the range of validity and performance of the model. Possibilities for improvements in yield and productivity could be deduced by model computations.",
author = "J. Bader and Bellgardt, {K. H.} and K. Sch{\"u}gerl",
note = "Funding Information: J B gratefully acknowledges financial assu&nce from Stiftung Stlpendlenfonds der Verbandes der Chemlschen Industne (FCI), Germany and the support of Professor H. Voss, Instltut fur Blotechnologie der Rheuusch-Westfahschen Techmschen Hochs-chule Aachen",
year = "1993",
month = aug,
doi = "10.1016/0300-9467(93)80045-P",
language = "English",
volume = "52",
pages = "B13--B19",
journal = "The Chemical Engineering Journal",
issn = "0300-9467",
publisher = "Elsevier",
number = "1",

}

Download

TY - JOUR

T1 - Modelling and simulation of the enzymatic hydrolysis of potato pulp by a complex enzyme mixture

AU - Bader, J.

AU - Bellgardt, K. H.

AU - Schügerl, K.

N1 - Funding Information: J B gratefully acknowledges financial assu&nce from Stiftung Stlpendlenfonds der Verbandes der Chemlschen Industne (FCI), Germany and the support of Professor H. Voss, Instltut fur Blotechnologie der Rheuusch-Westfahschen Techmschen Hochs-chule Aachen

PY - 1993/8

Y1 - 1993/8

N2 - The enzymatic hydrolysis of potato pulp by a cell-free culture filtrate of Trichoderma reesei Rut C30 was studied. On the basis of the experimental data a dynamic unstructured model using Michaelis-Menten kinetics was developed. This mathematical model describes the enzymatic hydrolysis in terms of the adsorption and desorption of enzymes on the solid substrate and with regard to competitive and uncompetitive inhibition. The model equations consist of a non-linear system of ordinary differential and algebraic equations. Parameter identification was done by dividing the model into submodels and fitting these to experimental data. The simulation results with the model correspond well with the experimental data. Thus the good agreement between simulated and measured process variables indicates that the model is suitable for description of the enzymatic hydrolysis. Computations for different operational conditions show the range of validity and performance of the model. Possibilities for improvements in yield and productivity could be deduced by model computations.

AB - The enzymatic hydrolysis of potato pulp by a cell-free culture filtrate of Trichoderma reesei Rut C30 was studied. On the basis of the experimental data a dynamic unstructured model using Michaelis-Menten kinetics was developed. This mathematical model describes the enzymatic hydrolysis in terms of the adsorption and desorption of enzymes on the solid substrate and with regard to competitive and uncompetitive inhibition. The model equations consist of a non-linear system of ordinary differential and algebraic equations. Parameter identification was done by dividing the model into submodels and fitting these to experimental data. The simulation results with the model correspond well with the experimental data. Thus the good agreement between simulated and measured process variables indicates that the model is suitable for description of the enzymatic hydrolysis. Computations for different operational conditions show the range of validity and performance of the model. Possibilities for improvements in yield and productivity could be deduced by model computations.

UR - http://www.scopus.com/inward/record.url?scp=0027639456&partnerID=8YFLogxK

U2 - 10.1016/0300-9467(93)80045-P

DO - 10.1016/0300-9467(93)80045-P

M3 - Article

AN - SCOPUS:0027639456

VL - 52

SP - B13-B19

JO - The Chemical Engineering Journal

JF - The Chemical Engineering Journal

SN - 0300-9467

IS - 1

ER -