Continuous production of (R)-phenylacetylcarbinol in an enzyme-membrane reactor using a potent mutant of pyruvate decarboxylase from Zymomonas mobilis

被引:35
|
作者
Goetz, G
Iwan, P
Hauer, B
Breuer, M
Pohl, M [1 ]
机构
[1] Univ Dusseldorf, Forschungszentrum Julich, Inst Enzymtechnol, D-52426 Julich, Germany
[2] BASF AG, D-67056 Ludwigshafen, Germany
关键词
pyruvate decarboxylase; biotransformation; carboligation; kinetic investigation;
D O I
10.1002/bit.1122.abs
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 optimization of a continuous enzymatic reaction yielding (R)-phenylacetylcarbinol (PAC), an intermediate of the L-ephedrine synthesis, is presented. We compare the suitability of three pyruvate decarboxylases (PDC), PDC from Saccharomyces cerevisiae, PDC from Zymomonas mobilis, and a potent mutant of the latter, PDCW392M, with respect to their application in the biotransformation using acetaldehyde and benzaldehyde as substrates. Among these, the mutant enzyme was the most active and most stable one. The reaction conditions of the carboligation reaction were investigated by determining initial rate velocities with varying substrate concentrations of both aldehydes. From the resulting data a kinetic model was inferred which fits the experimental data with sufficient reliability to deduce the optimal concentrations of both substrates for the enzymatic process. The results demonstrate that the carboligation is most efficiently performed using a continuous reaction system and feeding both aldehydes in equimolar concentration. Initial studies using a continuously operated enzyme-membrane reactor gave (R)-PAC with a space-time yield of 81 g L-1 d(-1) using a substrate concentration of 50 mM of both aldehydes. The yield was easily increased by cascadation of enzyme-membrane reactors. The new strategy allows the synthesis of (R)-PAC from cheap substrates in an aqueous reaction system. It thereby overcomes the limitation of by-product formation that severely limits the current fermentative process. (C) 2001 John Wiley & Sons, Inc.
引用
收藏
页码:317 / 325
页数:9
相关论文
共 39 条
  • [21] CONTINUOUS PRODUCTION OF GLUCONIC ACID AND SORBITOL FROM SUCROSE USING INVERTASE AND AN OXIDOREDUCTASE OF ZYMOMONAS-MOBILIS
    RO, HS
    KIM, HS
    ENZYME AND MICROBIAL TECHNOLOGY, 1991, 13 (11) : 920 - 924
  • [22] CONTINUOUS ETHANOL-PRODUCTION FROM SAGO STARCH USING IMMOBILIZED AMYLOGLUCOSIDASE AND ZYMOMONAS-MOBILIS
    LEE, GM
    KIM, CH
    ABIDIN, Z
    HAN, MH
    RHEE, SK
    JOURNAL OF FERMENTATION TECHNOLOGY, 1987, 65 (05): : 531 - 535
  • [23] Continuous production of pectic oligosaccharides from onion skins with an enzyme membrane reactor
    Baldassarre, Stefania
    Babbar, Neha
    Van Roy, Sandra
    Dejonghe, Winnie
    Maesen, Miranda
    Sforza, Stefano
    Elst, Kathy
    FOOD CHEMISTRY, 2018, 267 : 101 - 110
  • [24] Continuous production of oligosaccharides from whey using a membrane reactor
    Foda, MI
    Lopez-Leiva, M
    PROCESS BIOCHEMISTRY, 2000, 35 (06) : 581 - 587
  • [25] PRODUCTION OF HIGH ETHANOL CONCENTRATIONS FROM GLUCOSE USING ZYMOMONAS-MOBILIS ENTRAPPED IN A VERTICAL ROTATING IMMOBILIZED CELL REACTOR
    AMIN, G
    DOELLE, HW
    ENZYME AND MICROBIAL TECHNOLOGY, 1990, 12 (06) : 443 - 446
  • [26] PRODUCTION OF HIGH ETHANOL CONCENTRATIONS FROM GLUCOSE USING A VERTICAL ROTATING IMMOBILIZED CELL REACTOR OF THE BACTERIUM ZYMOMONAS-MOBILIS
    AMIN, G
    DOELLE, HW
    ACTA BIOTECHNOLOGICA, 1990, 10 (01): : 35 - 40
  • [27] CONTINUOUS PRODUCTION OF GLUCONIC ACID AND SORBITOL FROM JERUSALEM-ARTICHOKE AND GLUCOSE USING AN OXIDOREDUCTASE OF ZYMOMONAS-MOBILIS AND INULINASE
    KIM, DM
    KIM, HS
    BIOTECHNOLOGY AND BIOENGINEERING, 1992, 39 (03) : 336 - 342
  • [28] Continuous production of sialyllactose from colominic acid using a membrane reactor
    Masuda, M
    Kawase, Y
    Kawase, M
    JOURNAL OF BIOSCIENCE AND BIOENGINEERING, 2000, 89 (02) : 119 - 125
  • [29] Continuous production of pectic oligosaccharides from sugar beet pulp in a cross flow continuous enzyme membrane reactor
    Kathy Elst
    Neha Babbar
    Sandra Van Roy
    Stefania Baldassarre
    Winnie Dejonghe
    Miranda Maesen
    Stefano Sforza
    Bioprocess and Biosystems Engineering, 2018, 41 : 1717 - 1729
  • [30] Continuous production of pectic oligosaccharides from sugar beet pulp in a cross flow continuous enzyme membrane reactor
    Elst, Kathy
    Babbar, Neha
    Van Roy, Sandra
    Baldassarre, Stefania
    Dejonghe, Winnie
    Maesen, Miranda
    Sforza, Stefano
    BIOPROCESS AND BIOSYSTEMS ENGINEERING, 2018, 41 (11) : 1717 - 1729