A comparison between batch and fed-batch simultaneous saccharification and fermentation of steam pretreated spruce

被引:141
作者
Rudolf, A [1 ]
Alkasrawi, M [1 ]
Zacchi, G [1 ]
Lidén, G [1 ]
机构
[1] Lund Univ, Dept Chem Engn, SE-22100 Lund, Sweden
关键词
ethanol; yeast; fermentation; enzymatic hydrolysis; spruce;
D O I
10.1016/j.enzmictec.2005.02.013
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
In order to improve the process economy it is important to use as high dry matter content as possible in simultaneous saccharification and fermentation (SSF). However, too high dry matter content often gives rise to severe inhibition of the yeast metabolism, due to the increased levels of toxic compounds. The aim of the present work was to increase the fibrous content in SSF of steam pretreated spruce to 10% by adapting the yeast to the inhibitory substrate and by using a fed-batch process. Both batch and fed-batch approaches were evaluated. The fed-batch experiments were started with a batch fermentation containing 6% dry matter. Fibrous slurry from the pretreatment was then added four times during the first 24 h giving a final dry matter content corresponding to 10%. The yeast used in the fermentation was produced aerobically on the hemicellulose hydrolysate obtained from the pretreatment. SSF batch and fed-batch experiments with a cell mass concentration of 2, 3 and 5 g/L were carried out. When adapted yeast was used, the available hexoses were completely converted within 72 h and the final ethanol concentrations reached 40-44 g/L. No major differences in performance between batch and fed-batch were seen, but the ethanol productivity during the first 24 h was higher in the fed-batch SSF experiments, particularly during the experiments with a cell mass concentration of 2 and 3 g/L. (c) 2005 Elsevier Inc. All rights reserved.
引用
收藏
页码:195 / 204
页数:10
相关论文
共 33 条
[1]   Recirculation of process streams in fuel ethanol production from softwood based on simultaneous saccharification and fermentation [J].
Alkasrawi, M ;
Galbe, M ;
Zacchi, G .
APPLIED BIOCHEMISTRY AND BIOTECHNOLOGY, 2002, 98 (1-9) :849-861
[2]  
AZHAR AF, 1981, BIOTECHNOL BIOEN S11, P293
[3]   Ethanol production from paper material using a simultaneous saccharification and fermentation system in a fed-batch basis [J].
Ballesteros, M ;
Oliva, JM ;
Manzanares, P ;
Negro, MJ ;
Ballesteros, I .
WORLD JOURNAL OF MICROBIOLOGY & BIOTECHNOLOGY, 2002, 18 (06) :559-561
[4]  
BANERJEE N, 1976, P ANN CONV SUG TECHN, V41, pG75
[5]   THE EFFECTS OF FURFURAL ON ETHANOL-PRODUCTION BY SACCHAROMYCES-CEREVISIAE IN BATCH CULTURE [J].
BOYER, LJ ;
VEGA, JL ;
KLASSON, KT ;
CLAUSEN, EC ;
GADDY, JL .
BIOMASS & BIOENERGY, 1992, 3 (01) :41-48
[6]   Effect of inhibitors released during steam-explosion treatment of poplar wood on subsequent enzymatic hydrolysis and SSF [J].
Cantarella, M ;
Cantarella, L ;
Gallifuoco, A ;
Spera, A ;
Alfani, F .
BIOTECHNOLOGY PROGRESS, 2004, 20 (01) :200-206
[7]  
GILLERAN CT, 2004, THESIS NATL U IRELAN
[8]  
HAAGLUND E, 1951, CHEM WOOD, P324
[9]   Recirculation of process water in the production of ethanol from softwood [J].
Larsson, M ;
Galbe, M ;
Zacchi, G .
BIORESOURCE TECHNOLOGY, 1997, 60 (02) :143-151
[10]   The generation of fermentation inhibitors during dilute acid hydrolysis of softwood [J].
Larsson, S ;
Palmqvist, E ;
Hahn-Hägerdal, B ;
Tengborg, C ;
Stenberg, K ;
Zacchi, G ;
Nilvebrant, NO .
ENZYME AND MICROBIAL TECHNOLOGY, 1999, 24 (3-4) :151-159