A comparison of liquid hot water and steam pretreatments of sugar cane bagasse for bioconversion to ethanol

被引:394
作者
Laser, M
Schulman, D
Allen, SG
Lichwa, J
Antal, MJ
Lynd, LR [1 ]
机构
[1] Dartmouth Coll, Thayer Sch Engn, Hanover, NH 03755 USA
[2] Univ Hawaii, Hawaii Nat Energy Inst, Honolulu, HI 96822 USA
关键词
liquid hot water; steam; pretreatment; sugar cane bagasse; bioconversion; ethanol;
D O I
10.1016/S0960-8524(01)00103-1
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
Sugar cane bagasse was pretreated with either liquid hot water (LHW) or steam using the same 251 reactor. Solids concentration ranged from 1% to 8% for LHW pretreatment and was greater than or equal to 50% for steam pretreatment. Reaction temperature and time ranged from 170 to 230 degreesC and 1 to 46 min, respectively. Key performance metrics included fiber reactivity, xylan recovery, and the extent to which pretreatment hydrolyzate inhibited glucose fermentation. In four cases, LHW pretreatment achieved greater than or equal to 80% conversion by simultaneous saccharification and fermentation (SSF), greater than or equal to 80% xylan recovery, and no hydrolyzate inhibition of glucose fermentation yield. Combined effectiveness was not as good for steam pretreatment due to low xylan recovery. SSF conversion increased and xylan recovery decreased as xylan dissolution increased for both modes. SSF conversion, xylan dissolution, hydrolyzate furfural concentration, and hydrolyzate inhibition increased, while xylan recovery and hydrolyzate pH decreased, as a function of increasing LHW pretreatment solids concentration (14%). These results are consistent with the notion that autohydrolysis. plays an important, if not exclusive, role in batch hydrothermal pretreatment. Achieving concurrently high (greater than 90%) SSF conversion and xylan recovery will likely require a modified reactor configuration (e.g. continuous percolation or base addition) that better preserves dissolved xylan. (C) 2001 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:33 / 44
页数:12
相关论文
共 37 条
[1]   A comparison between hot liquid water and steam fractionation of corn fiber [J].
Allen, SG ;
Schulman, D ;
Lichwa, J ;
Antal, MJ ;
Laser, M ;
Lynd, LR .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2001, 40 (13) :2934-2941
[2]   Fractionation of sugar cane with hot, compressed, liquid water [J].
Allen, SG ;
Kam, LC ;
Zemann, AJ ;
Antal, MJ .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1996, 35 (08) :2709-2715
[3]  
ALLEN SG, 1997, DEV THERMOCHEMICAL B, P765
[4]   HYDROTHERMAL DEGRADATION OF POLYMERS DERIVED FROM PLANTS [J].
BOBLETER, O .
PROGRESS IN POLYMER SCIENCE, 1994, 19 (05) :797-841
[5]  
BOBLETER O, 1991, STEAM EXPLOSION TECH, P59
[6]   HYDROTHERMAL AND ORGANOSOLV PRETREATMENTS OF POPLAR WOOD AND WHEAT STRAW FOR SACCHARIFICATION BY A TRICHODERMA-VIRIDE CELLULASE [J].
BONN, G ;
HORMEYER, HF ;
BOBLETER, O .
WOOD SCIENCE AND TECHNOLOGY, 1987, 21 (02) :179-185
[7]   ANALYTICAL METHODOLOGY FOR BIOMASS PRETREATMENT .2. CHARACTERIZATION OF THE FILTRATES AND CUMULATIVE PRODUCT DISTRIBUTION AS A FUNCTION OF TREATMENT SEVERITY [J].
BOUCHARD, J ;
NGUYEN, TS ;
CHORNET, E ;
OVEREND, RP .
BIORESOURCE TECHNOLOGY, 1991, 36 (02) :121-131
[8]   KINETICS OF THERMOCHEMICAL PRETREATMENT OF LIGNOCELLULOSIC MATERIALS [J].
CONVERSE, AO ;
KWARTENG, IK ;
GRETHLEIN, HE ;
OOSHIMA, H .
APPLIED BIOCHEMISTRY AND BIOTECHNOLOGY, 1989, 20-1 :63-78
[9]  
CONVERSE AO, 1993, BIOCONVERSION FOREST, pCH4
[10]   Hydrolysis of lignocellulosics at low enzyme levels: Application of the AFEX process [J].
Dale, BE ;
Leong, CK ;
Pham, TK ;
Esquivel, VM ;
Rios, I ;
Latimer, VM .
BIORESOURCE TECHNOLOGY, 1996, 56 (01) :111-116