Details
Original language | English |
---|---|
Pages (from-to) | 653-660 |
Number of pages | 8 |
Journal | Enzyme and microbial technology |
Volume | 28 |
Issue number | 7-8 |
Publication status | Published - 1 May 2001 |
Abstract
A new experimental high-pressure-unit was constructed for the enantioselective enzymatic hydrolysis of 3-hydroxy-5-phenyl-4-pentenoicacidethylester (a precursor for biological interesting substances) in a biphasic buffer/SCCO2-system. One objective is to take advantage of the solubility differences of the substrate and the produced acid. Thus the different solubilities of the substrates and the products in the different phases were studied regarding to an overall process integration. One ester enantiomer is preferably hydrolyzed, the other remains in the supercritical phase. And the produced acid enantiomer is concentrated in the buffer phase. The decrease in pressure is followed by an extraction process of the remaining substrate-enantiomer, in consequence it will be possible to combine an enzymatic reaction with a separation step. The catalysis was optimized in regard to enantioselectivity, enantiomeric excess, conversion and reaction time. A high enantioselectivity is achieved for the aromatic substrate using the lipase of Pseudomonas cepacia. The results show that this unconventional reaction system offers tremendous advantages for enzyme process development.
ASJC Scopus subject areas
- Biochemistry, Genetics and Molecular Biology(all)
- Biotechnology
- Chemical Engineering(all)
- Bioengineering
- Biochemistry, Genetics and Molecular Biology(all)
- Biochemistry
- Immunology and Microbiology(all)
- Applied Microbiology and Biotechnology
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In: Enzyme and microbial technology, Vol. 28, No. 7-8, 01.05.2001, p. 653-660.
Research output: Contribution to journal › Article › Research › peer review
}
TY - JOUR
T1 - The enantioselective hydrolysis of 3-hydroxy-5-phenyl-4-pentenoicacidethylester in supercritical carbon dioxide using lipases
AU - Hartmann, T.
AU - Meyer, H. H.
AU - Scheper, T.
N1 - Funding information: This work was financially supported by the Deutsche Forschungsgemeinschaft (Graduiertenkolleg: “Chemische und Technische Grundlagen der Naturstofftransformation”). The authors are grateful to “AMANO Enzymes” for kindly providing us with the gift of PSL.
PY - 2001/5/1
Y1 - 2001/5/1
N2 - A new experimental high-pressure-unit was constructed for the enantioselective enzymatic hydrolysis of 3-hydroxy-5-phenyl-4-pentenoicacidethylester (a precursor for biological interesting substances) in a biphasic buffer/SCCO2-system. One objective is to take advantage of the solubility differences of the substrate and the produced acid. Thus the different solubilities of the substrates and the products in the different phases were studied regarding to an overall process integration. One ester enantiomer is preferably hydrolyzed, the other remains in the supercritical phase. And the produced acid enantiomer is concentrated in the buffer phase. The decrease in pressure is followed by an extraction process of the remaining substrate-enantiomer, in consequence it will be possible to combine an enzymatic reaction with a separation step. The catalysis was optimized in regard to enantioselectivity, enantiomeric excess, conversion and reaction time. A high enantioselectivity is achieved for the aromatic substrate using the lipase of Pseudomonas cepacia. The results show that this unconventional reaction system offers tremendous advantages for enzyme process development.
AB - A new experimental high-pressure-unit was constructed for the enantioselective enzymatic hydrolysis of 3-hydroxy-5-phenyl-4-pentenoicacidethylester (a precursor for biological interesting substances) in a biphasic buffer/SCCO2-system. One objective is to take advantage of the solubility differences of the substrate and the produced acid. Thus the different solubilities of the substrates and the products in the different phases were studied regarding to an overall process integration. One ester enantiomer is preferably hydrolyzed, the other remains in the supercritical phase. And the produced acid enantiomer is concentrated in the buffer phase. The decrease in pressure is followed by an extraction process of the remaining substrate-enantiomer, in consequence it will be possible to combine an enzymatic reaction with a separation step. The catalysis was optimized in regard to enantioselectivity, enantiomeric excess, conversion and reaction time. A high enantioselectivity is achieved for the aromatic substrate using the lipase of Pseudomonas cepacia. The results show that this unconventional reaction system offers tremendous advantages for enzyme process development.
UR - http://www.scopus.com/inward/record.url?scp=0035820860&partnerID=8YFLogxK
U2 - 10.1016/S0141-0229(01)00313-1
DO - 10.1016/S0141-0229(01)00313-1
M3 - Article
AN - SCOPUS:0035820860
VL - 28
SP - 653
EP - 660
JO - Enzyme and microbial technology
JF - Enzyme and microbial technology
SN - 0141-0229
IS - 7-8
ER -