Microbial reduction and in situ product crystallization coupled with biocatalyst cultivation during the synthesis of 6R-dihydrooxoisophorone

被引:15
作者
Buque-Taboada, EM
Straathof, AJJ
Heijnen, JJ
van der Wielen, LAM
机构
[1] Delft Univ Technol, Dept Biotechnol, NL-2628 BC Delft, Netherlands
[2] Univ San Carlos, Dept Chem Engn, Cebu 6000, Philippines
关键词
crystallization; 6R-dihydrooxoisophorone; in situ product recovery; 4-oxoisophorone; reduction; Saccharomyces cerevisiae;
D O I
10.1002/adsc.200505024
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
An in situ product crystallization procedure was developed for a crystalline product formed during microbial reduction coupled with cell cultivation. The model reaction was the asymmetric reduction of 4-oxoisophorone (OIP) by baker's yeast (Saccharomyces cerevisiae). Yeast cells were cultivated fed-batch to reach a maximum concentration of 30 gdw center dot L-1. The desired product, 6R-dihydrooxoisophorone (DOIP), may be further reduced by baker's yeast to an unwanted by-product; thus, DOIP was removed immediately from the fermenter via an external crystallization loop in this procedure. The OIP reduction rate was five times higher (congruent to 0.33 mmol center dot gdw(-1)center dot h(-1)) as compared to the reduction rate with resting cells. OIP reduction was started when the optimum cell concentration had already been reached in the reactor because the substrate (OIP) at >= 55 mM concentration inhibited cell growth. An appropriate supply of glucose as carbon and energy source was necessary to support the coupled reactions involving cell growth and maintenance and product formation while avoiding formation of metabolic by-products. Final DOIP yield and selectivity were 85% and 99%, respectively, while over 100 g center dot L-1 of product was obtained in the crystallizer. The product crystals with favorable properties were readily recovered from the crystallizer. These results indicate that product crystallization is not impaired by the solutes present in the fermentation medium.
引用
收藏
页码:1147 / 1154
页数:8
相关论文
共 29 条
[1]   Optimal operation of an integrated bioreaction-crystallization process for continuous production of calcium gluconate using external loop airlift columns [J].
Bao, J ;
Koumatsu, K ;
Furumoto, K ;
Yoshimoto, M ;
Fukunaga, K ;
Nakao, K .
CHEMICAL ENGINEERING SCIENCE, 2001, 56 (21-22) :6165-6170
[2]  
Beudeker R. F., 1990, YEAST BIOTECHNOLOGY, P103
[3]   Immobilization affects the rate and enantioselectivity of 3-oxo ester reduction by baker's yeast [J].
Buque, EM ;
Chin-Joe, I ;
Straathof, AJJ ;
Jongejan, JA ;
Heijnen, JJ .
ENZYME AND MICROBIAL TECHNOLOGY, 2002, 31 (05) :656-664
[4]   In situ product removal using a crystallization loop in asymmetric reduction of 4-oxoisophorone by Saccharomyces cerevisiae [J].
Buque-Taboada, EM ;
Straathof, AJJ ;
Heijnen, JJ ;
van der Wielen, LAM .
BIOTECHNOLOGY AND BIOENGINEERING, 2004, 86 (07) :795-800
[5]  
BUQUETABOADA EM, 2005, IN PRESS ENZYME MICR
[6]   A SIMPLE-MODEL FOR THE OPTIMIZATION OF THE EXTRACTION YIELD OF ANTIBIOTICS ISOLATED FROM FERMENTED BROTHS BY DIRECT CRYSTALLIZATION [J].
CARDOSO, JP .
BIOTECHNOLOGY AND BIOENGINEERING, 1993, 42 (09) :1068-1076
[7]  
Chen S. L., 1985, COMPREHENSIVE BIOTEC, P429
[8]   Influence of the ethanol and glucose supply rate on the rate and enantioselectivity of 3-oxo ester reduction by baker's yeast [J].
Chin-Joe, I ;
Straathof, AJJ ;
Pronk, JT ;
Jongejan, JA ;
Heijnen, JJ .
BIOTECHNOLOGY AND BIOENGINEERING, 2001, 75 (01) :29-38
[9]  
Darrigo P, 1997, ADV APPL MICROBIOL, V44, P81, DOI 10.1016/S0065-2164(08)70460-X
[10]  
Furui M., 1988, BIOCATALYSIS, V2, P69