Extractive bioconversion of 2-phenylethanol from L-phenylalanine by Saccharomyces cerevisiae

被引:139
作者
Stark, D
Münch, T
Sonnleitner, B
Marison, IW
von Stockar, U [1 ]
机构
[1] Swiss Fed Inst Technol, Lab Chem & Biochem Engn, CH-1015 Lausanne, Switzerland
[2] Givaudan Dubendorf Ltd, Dubendorf, Switzerland
[3] Zurich Univ Appl Sci, Dept Chem, CH-8400 Winterthur, Switzerland
关键词
D O I
10.1021/bp020006n
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
The bioconversion of L-phenylalanine (L-Phe) to 2-phenylethanol (PEA) by the yeast Saccharomyces cerevisiae is limited by the toxicity of the product. PEA extraction by a separate organic phase in the fermenter is the ideal in situ product recovery (ISPR) technique to enhance productivity. Oleic acid was chosen as organic phase for two-phase fed-batch cultures, although it interfered to some extent with yeast viability. There was a synergistic inhibitory impact toward S. cerevisiae in the presence of PEA, and therefore a maximal PEA concentration in the aqueous phase of only 2.1 g/L was achieved, compared to 3.8 g/L for a normal fed-batch culture. However, the overall PEA concentration in the fermenter was increased to 12.6 g/L, because the PEA concentration in the oleic phase attained a value of 24 g/L. Thus, an average volumetric PEA production rate of 0.26 g L-1 h(-1) and a maximal volumetric PEA production rate of 0.47 g L-1 h(-1) were achieved in the two-phase fed-batch culture. As ethanol inhibition had to be avoided, the production rates were limited by the intrinsic oxidative capacity of S. cerevisiae. In addition, the high viscosity of the two-phase system lowered the k(1)a, and therefore also the productivity. Thus, if a specific ISPR technique is planned, it consequently has to be remembered that the productivity of this bioconversion process is also quickly limited by the k(1)a of the fermenter at high cell densities.
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页码:514 / 523
页数:10
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