Production of ethanol by immobilised whole cells of Zymomonas mobilis in an expanded bed bioreactor

被引:11
作者
Kesava, SS [1 ]
Panda, T [1 ]
Rakshit, SK [1 ]
机构
[1] INDIAN INST TECHNOL, DEPT CHEM ENGN, BIOTECHNOL RES CTR, MADRAS 600036, TAMIL NADU, INDIA
关键词
D O I
10.1016/0032-9592(95)00086-0
中图分类号
Q5 [生物化学]; Q7 [分子生物学];
学科分类号
071010 ; 081704 ;
摘要
Whole cells of Zymomonas mobilis, immobilised on pectin beads, were stablised by curing in a mixture of 0.2 M CaCl2 .2H2O and Na2B4O7 . 10H(2)O for 24 h at 4 degrees C. Ethanol fermentation was studied using different glucose concentrations (50-200 g/litre) by these immobilised beads. The kinetics of this process was studied in a glucose step-feeding system with different total glucose concentrations (150 and 200 g/litre) in a specially designed shake flask. Immobilised whole cells were also used for ethanol fermentation in an expanded bed bioreactor and its performance characteristics were compared with those of a regular batch mechanically stirred tank bioreactor Fermentation rates and ethanol yields were higher in the expanded bed bioreactor system than in the batch mechanically agitated stirred tank bioreactor The stabilised pectin beads were damaged less in the expanded bioreactor than in the regular batch stirred tank reactor.
引用
收藏
页码:449 / 456
页数:8
相关论文
共 22 条
[1]  
ACOSTA S, 1988, MIRCEN Journal of Applied Microbiology and Biotechnology, V4, P221, DOI 10.1007/BF01301951
[2]   CHARACTERISTICS OF IMMOBILIZED YEAST REACTORS PRODUCING ETHANOL FROM GLUCOSE [J].
ANSELME, MJ ;
TEDDER, DW .
BIOTECHNOLOGY AND BIOENGINEERING, 1987, 30 (06) :736-745
[3]   METHANOGENESIS FROM VOLATILE FATTY-ACIDS IN DOWNFLOW STATIONARY FIXED-FILM REACTOR [J].
BHADRA, A ;
SCHARER, JM ;
MOOYOUNG, M .
BIOTECHNOLOGY AND BIOENGINEERING, 1987, 30 (02) :314-319
[4]   PRACTICAL REACTOR SYSTEMS FOR YEAST-CELL IMMOBILIZATION USING BIOMASS SUPPORT PARTICLES [J].
BLACK, GM ;
WEBB, C ;
MATTHEWS, TM ;
ATKINSON, B .
BIOTECHNOLOGY AND BIOENGINEERING, 1984, 26 (02) :134-141
[5]   MODELING ETHANOL AND SECONDARY INHIBITIONS OF ETHANOL FERMENTATION IN A MULTISTAGE REACTOR [J].
CHATTAWAY, T ;
GOMA, G ;
RENAUD, PY .
BIOTECHNOLOGY AND BIOENGINEERING, 1988, 32 (03) :271-276
[6]   OPERABILITY AND FEASIBILITY OF ETHANOL-PRODUCTION BY IMMOBILIZED ZYMOMONAS-MOBILIS IN A FLUIDIZED-BED BIOREACTOR [J].
DAVISON, BH ;
SCOTT, CD .
APPLIED BIOCHEMISTRY AND BIOTECHNOLOGY, 1988, 18 :19-34
[7]   MODELING AND STATIC OPTIMIZATION OF THE ETHANOL-PRODUCTION IN A CASCADE REACTOR .2. STATIC OPTIMIZATION [J].
DOURADO, A ;
CALVET, JL ;
SEVELY, Y ;
GOMA, G .
BIOTECHNOLOGY AND BIOENGINEERING, 1987, 29 (02) :195-203
[8]   CONTINUOUS EXTRACTION LOOP REACTOR (CELR) - ALCOHOLIC FERMENTATION BY FLUIDIZED ENTRAPPED BIOMASS [J].
GIANETTO, A ;
RUGGERI, B ;
SPECCHIA, V ;
SASSI, G ;
FORNA, R .
CHEMICAL ENGINEERING SCIENCE, 1988, 43 (08) :1891-1896
[9]   CONTINUOUS ETHANOL PRODUCTION BY IMMOBILIZED CELLS OF ZYMOMONAS-MOBILIS [J].
GROTE, W ;
LEE, KJ ;
ROGERS, PL .
BIOTECHNOLOGY LETTERS, 1980, 2 (11) :481-486
[10]   PERFORMANCE OF TAPERED COLUMN PACKED-BED BIOREACTOR FOR ETHANOL-PRODUCTION [J].
HAMAMCI, H ;
RYU, DDY .
BIOTECHNOLOGY AND BIOENGINEERING, 1987, 29 (08) :994-1002