Pretreatment of Rice Straw by a Hot-Compressed Water Process for Enzymatic Hydrolysis

被引:139
作者
Yu, Guoce [1 ,2 ]
Yano, Shinichi [2 ]
Inoue, Hiroyuki [2 ]
Inoue, Seiichi [2 ]
Endo, Takashi [2 ]
Sawayama, Shigeki [2 ]
机构
[1] Tsinghua Univ, Inst Nucl & New Energy Technol, Beijing 100084, Peoples R China
[2] Natl Inst Adv Ind Sci & Technol, Biomass Technol Res Ctr, Hiroshima 7370197, Japan
关键词
Rice straw; Pretreatment; Hot-compressed water; Sugar production; Inhibitor formation; Enzymatic hydrolysis; Fermentation; SUGAR-CANE BAGASSE; PRESSURE COOKING; CORN FIBER; HYDROTHERMAL DEGRADATION; ETHANOL-PRODUCTION; LIQUID; FRACTIONATION; HEMICELLULOSE; BIOMASS; SACCHARIFICATION;
D O I
10.1007/s12010-008-8420-z
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
Hot-compressed water (HCW) is among several cost-effective pretreatment processes of lignocellulosic biomass for enzymatic hydrolysis. The present work investigated the characteristics of HCW pretreatment of rice straw including sugar production and inhibitor formation in the liquid fraction and enzymatic hydrolysis of pretreated material. Pretreatment was carried out at a temperature ranging from 140 to 240 A degrees C for 10 or 30 min. Soluble oligosaccharides were found to constitute almost all the components of total sugars in the liquid fraction. The maximal production of total glucose at 180 A degrees C and below accounted for 4.4-4.9% of glucan in raw material. Total xylose production peaked at 180 A degrees C, accounting for 43.3% of xylan in raw material for 10-min pretreatment and 29.8% for 30-min pretreatment. The production of acetic acid increased at higher temperatures and longer treatment time, indicating more significant disruption of lignocellulosic structure, and furfural production achieved the maximum (2.8 mg/ml) at 200 A degrees C for both 10-min and 30-min processes. The glucose yield by enzymatic hydrolysis of pretreated rice straw was no less than 85% at 180 A degrees C and above for 30-min pretreatment and at 200 A degrees C and above for 10-min pretreatment. Considering sugar recovery, inhibitor formation, and process severity, it is recommended that a temperature of 180 A degrees C for a time of 30 min can be the most efficient process for HCW pretreatment of rice straw.
引用
收藏
页码:539 / 551
页数:13
相关论文
共 27 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]   Decomposition behavior of plant biomass in hot-compressed water [J].
Ando, H ;
Sakaki, T ;
Kokusho, T ;
Shibata, M ;
Uemura, Y ;
Hatate, Y .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2000, 39 (10) :3688-3693
[4]   HYDROTHERMAL DEGRADATION OF CELLULOSIC MATTER TO SUGARS AND THEIR FERMENTATIVE CONVERSION TO PROTEIN [J].
BOBLETER, O ;
NIESNER, R ;
ROHR, M .
JOURNAL OF APPLIED POLYMER SCIENCE, 1976, 20 (08) :2083-2093
[5]   HYDROTHERMAL DEGRADATION OF POLYMERS DERIVED FROM PLANTS [J].
BOBLETER, O .
PROGRESS IN POLYMER SCIENCE, 1994, 19 (05) :797-841
[6]  
Bobleter O., 1979, Cellul. Chem. Technol, V13, P583
[7]   Liquid hot water pretreatment of olive tree pruning residues [J].
Cara, Cristobal ;
Romero, Inmaculada ;
Miguel Oliva, Jose ;
Saez, Felicia ;
Castro, Eulogio .
APPLIED BIOCHEMISTRY AND BIOTECHNOLOGY, 2007, 137 (1-12) :379-394
[8]   Enzymatic saccharification of hot-water pretreated corn fiber for production of monosaccharides [J].
Dien, B. S. ;
Li, X. -L. ;
Iten, L. B. ;
Jordan, D. B. ;
O'Bryan, P. J. ;
Cotta, M. A. .
ENZYME AND MICROBIAL TECHNOLOGY, 2006, 39 (05) :1137-1144
[9]  
HORMEYER HF, 1988, APPL MICROBIOL BIOT, V29, P528, DOI 10.1007/BF00260980
[10]   A comparison of liquid hot water and steam pretreatments of sugar cane bagasse for bioconversion to ethanol [J].
Laser, M ;
Schulman, D ;
Allen, SG ;
Lichwa, J ;
Antal, MJ ;
Lynd, LR .
BIORESOURCE TECHNOLOGY, 2002, 81 (01) :33-44