APPLICATION OF A MEMBRANE RECYCLE BIOREACTOR FOR CONTINUOUS ETHANOL-PRODUCTION

被引:32
作者
MELZOCH, K
RYCHTERA, M
MARKVICHOV, NS
POSPICHALOVA, V
BASAROVA, G
MANAKOV, MN
机构
[1] PRAGUE INST CHEM TECHNOL, DEPT FERMENTAT CHEM & BIOENGN, CS-16628 PRAGUE, CZECHOSLOVAKIA
[2] DI MENDELEEV CHEM TECHNOL INST, DEPT IND BIOTECHNOL, MOSCOW, USSR
关键词
D O I
10.1007/BF00180572
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
A series of continuous fermentations were carried out with a production strain of the yeast Saccharomyces cerevisiae in a membrane bioreactor. A membrane separation module composed of ultrafiltration tubular membranes retained all biomass in a fermentation zone of the bioreactor and allowed continuous removal of fermentation products into a cell-free permeate. In a system with total (100%) cell recycle the impact of fermentation conditions [dilution rate (0.03-0.3 h-1); substrate concentration in the feed (50-300 g.l-1); biomass concentration (depending on the experimental conditions)] was studied on the behaviour of the "immobilized" cell population and on ethanol formation. Maximum ethanol productivity (15 g.l-1.h-1) was attained at an ethanol concentration of 81 g.l-1. The highest demands of cells for maintenance energy were found at the maximum feed substrate concentration (300 g.l-1 and at very low concentrations of cells in the broth.
引用
收藏
页码:469 / 472
页数:4
相关论文
共 22 条
[1]  
BOINOT F, 1936, Patent No. 630193
[2]  
CHERYAN M, 1984, PROCESS BIOCHEM, V19, P204
[3]  
DAMIANO D, 1985, APPL MICROBIOL BIOT, V21, P69
[4]   REACTION CHARACTERISTICS OF AN IMMOBILIZED YEAST PRODUCING ETHANOL [J].
FURUSAKI, S ;
SEKI, M ;
FUKUMURA, K .
BIOTECHNOLOGY AND BIOENGINEERING, 1983, 25 (12) :2921-2928
[5]  
GREGR V, 1966, ANAL METHODS LABORAT, V3
[6]   CONTINUOUS PRODUCTION OF BUTANOL FROM A GLUCOSE XYLOSE MIXTURE WITH AN IMMOBILIZED CELL SYSTEM COUPLED TO PERVAPORATION [J].
GROOT, WJ ;
LUYBEN, KCAM .
BIOTECHNOLOGY LETTERS, 1987, 9 (12) :867-870
[7]   PERVAPORATION FOR SIMULTANEOUS PRODUCT RECOVERY IN THE BUTANOL ISOPROPANOL BATCH FERMENTATION [J].
GROOT, WJ ;
VANDENOEVER, CE ;
KOSSEN, NWF .
BIOTECHNOLOGY LETTERS, 1984, 6 (11) :709-714
[8]   STEADY-STATE ANALYSIS OF THE ENHANCEMENT IN ETHANOL PRODUCTIVITY OF A CONTINUOUS FERMENTATION PROCESS EMPLOYING A PROTEIN-PHOSPHOLIPID COMPLEX AS A PROTECTING AGENT [J].
JIN, CK ;
CHIANG, HL ;
WANG, SS .
ENZYME AND MICROBIAL TECHNOLOGY, 1981, 3 (03) :249-257
[9]   PERFORMANCE OF AN IMMOBILIZED YEAST REACTOR SYSTEM FOR ETHANOL-PRODUCTION [J].
LEE, TH ;
AHN, JC ;
RYU, DDY .
ENZYME AND MICROBIAL TECHNOLOGY, 1983, 5 (01) :41-45
[10]   KINETICS OF ETHANOL INHIBITION IN ALCOHOL FERMENTATION [J].
LUONG, JHT .
BIOTECHNOLOGY AND BIOENGINEERING, 1985, 27 (03) :280-285