A kinetic study of lipase‐catalyzed reversible kinetic resolution involving verification at miniplant‐scale

Abstract Lipase‐catalyzed kinetic resolution of racemates is a popular method for synthesis of chiral synthons. Most of these resolutions are reversible equilibrium limited reactions. For the first time, an extensive kinetic model is proposed for kinetic resolution reactions, which takes into accoun...

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Published in:Biotechnology and Bioengineering
Main Authors: Berendsen, W.R., Gendrot, G., Freund, A., Reuss, M.
Format: Article in Journal/Newspaper
Language:English
Published: Wiley 2006
Subjects:
Online Access:http://dx.doi.org/10.1002/bit.21034
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spelling crwiley:10.1002/bit.21034 2024-06-02T07:58:38+00:00 A kinetic study of lipase‐catalyzed reversible kinetic resolution involving verification at miniplant‐scale Berendsen, W.R. Gendrot, G. Freund, A. Reuss, M. 2006 http://dx.doi.org/10.1002/bit.21034 https://api.wiley.com/onlinelibrary/tdm/v1/articles/10.1002%2Fbit.21034 https://onlinelibrary.wiley.com/doi/pdf/10.1002/bit.21034 en eng Wiley http://onlinelibrary.wiley.com/termsAndConditions#vor Biotechnology and Bioengineering volume 95, issue 5, page 883-892 ISSN 0006-3592 1097-0290 journal-article 2006 crwiley https://doi.org/10.1002/bit.21034 2024-05-03T11:09:11Z Abstract Lipase‐catalyzed kinetic resolution of racemates is a popular method for synthesis of chiral synthons. Most of these resolutions are reversible equilibrium limited reactions. For the first time, an extensive kinetic model is proposed for kinetic resolution reactions, which takes into account the full reversibility of the reaction, substrate inhibition by an acyl donor and an acyl acceptor as well as alternative substrate inhibition by each enantiomer. For this purpose, the reversible enantioselective transesterification of (R/S)‐1‐methoxy‐2‐propanol with ethyl acetate catalyzed by Candida antarctica lipase B (CAL‐B) is investigated. The detailed model presented here is valid for a wide range of substrate and product concentrations. Following model discrimination and the application of Haldane equations to reduce the degree of freedom in parameter estimation, the 11 free parameters are successfully identified. All parameters are fitted to the complete data set simultaneously. Six types of independent initial rate studies provide a solid data basis for the model. The effect of changes in substrate and product concentration on reaction kinetics is discussed. The developed model is used for simulations to study the behavior of reaction kinetics in a fixed bed reactor. The typical plot of enantiomeric excess versus conversion of substrate and product is evaluated at various initial substrate mixtures. The model is validated by comparison with experimental results obtained with a fixed bed reactor, which is part of a fully automated state‐of‐the‐art miniplant. © 2006 Wiley Periodicals, Inc. Article in Journal/Newspaper Antarc* Antarctica Wiley Online Library Biotechnology and Bioengineering 95 5 883 892
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language English
description Abstract Lipase‐catalyzed kinetic resolution of racemates is a popular method for synthesis of chiral synthons. Most of these resolutions are reversible equilibrium limited reactions. For the first time, an extensive kinetic model is proposed for kinetic resolution reactions, which takes into account the full reversibility of the reaction, substrate inhibition by an acyl donor and an acyl acceptor as well as alternative substrate inhibition by each enantiomer. For this purpose, the reversible enantioselective transesterification of (R/S)‐1‐methoxy‐2‐propanol with ethyl acetate catalyzed by Candida antarctica lipase B (CAL‐B) is investigated. The detailed model presented here is valid for a wide range of substrate and product concentrations. Following model discrimination and the application of Haldane equations to reduce the degree of freedom in parameter estimation, the 11 free parameters are successfully identified. All parameters are fitted to the complete data set simultaneously. Six types of independent initial rate studies provide a solid data basis for the model. The effect of changes in substrate and product concentration on reaction kinetics is discussed. The developed model is used for simulations to study the behavior of reaction kinetics in a fixed bed reactor. The typical plot of enantiomeric excess versus conversion of substrate and product is evaluated at various initial substrate mixtures. The model is validated by comparison with experimental results obtained with a fixed bed reactor, which is part of a fully automated state‐of‐the‐art miniplant. © 2006 Wiley Periodicals, Inc.
format Article in Journal/Newspaper
author Berendsen, W.R.
Gendrot, G.
Freund, A.
Reuss, M.
spellingShingle Berendsen, W.R.
Gendrot, G.
Freund, A.
Reuss, M.
A kinetic study of lipase‐catalyzed reversible kinetic resolution involving verification at miniplant‐scale
author_facet Berendsen, W.R.
Gendrot, G.
Freund, A.
Reuss, M.
author_sort Berendsen, W.R.
title A kinetic study of lipase‐catalyzed reversible kinetic resolution involving verification at miniplant‐scale
title_short A kinetic study of lipase‐catalyzed reversible kinetic resolution involving verification at miniplant‐scale
title_full A kinetic study of lipase‐catalyzed reversible kinetic resolution involving verification at miniplant‐scale
title_fullStr A kinetic study of lipase‐catalyzed reversible kinetic resolution involving verification at miniplant‐scale
title_full_unstemmed A kinetic study of lipase‐catalyzed reversible kinetic resolution involving verification at miniplant‐scale
title_sort kinetic study of lipase‐catalyzed reversible kinetic resolution involving verification at miniplant‐scale
publisher Wiley
publishDate 2006
url http://dx.doi.org/10.1002/bit.21034
https://api.wiley.com/onlinelibrary/tdm/v1/articles/10.1002%2Fbit.21034
https://onlinelibrary.wiley.com/doi/pdf/10.1002/bit.21034
genre Antarc*
Antarctica
genre_facet Antarc*
Antarctica
op_source Biotechnology and Bioengineering
volume 95, issue 5, page 883-892
ISSN 0006-3592 1097-0290
op_rights http://onlinelibrary.wiley.com/termsAndConditions#vor
op_doi https://doi.org/10.1002/bit.21034
container_title Biotechnology and Bioengineering
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