期刊文献+

采用稀盐酸和硝酸水解玉米芯产木糖及其优化 被引量:5

Kinetic Studies and Optimization of Dilute Hydrochloric Acid and Nitric Acid Hydrolysis of Corncob for Xylose Production
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摘要 采用稀HCl和HNO3在酸质量分数为1.0%、2.5%和4.0%,反应时间10、30、50、90和120min,温度90和150℃条件下,对玉米芯水解产木糖进行研究。通过动力学模型数据预测木糖浓度,并采用响应曲面优化各个温度下的水解条件。优化得到的最适宜水解条件为温度150℃,预处理时间10 min,酸质量分数为1.0%;对应HNO3得到的木糖浓度为56.77 g/L,产率96.31%;HCl木糖浓度为45.38 g/L,产率76.99%。动力学结果成功预测了反应条件下的木糖浓度。通过对比得出HNO3对玉米芯的水解效果要优于HCl。 Xylose production by hydrolysis of corncob with dilute hydrochloric acid and nitric acid were studied, in respect to temperature (90 - 150 ℃), acid concentration (1.0%, 2.5% and 4.0% ) and reaction time( 10 - 120 rain). Kinetic parameters of mathematical model for predicting the concentrations of xylose were found. The central composite 'design of response surface method was used to optimize the pretreatment conditions. The results showed that hydrolysis conditions for highest xylose production was 1.0% acid concentration for 10 rain at 150 ℃, corresponding to 96.31% (56.77 g/L) total xylan con- verted to xylose for nitric acid, 76.99% (45.38 g/L) for hydrochloric acid. The models could be suc- cessfully used to predict the concentrations of xylose under the experimental conditions. The results showed the hydrolysis effect of nitric acid was much better than that of hydrochloric acid.
出处 《化学工业与工程》 CAS 2013年第2期1-6,共6页 Chemical Industry and Engineering
基金 国家青年基金(21106097)
关键词 玉米芯 HCL HNO3 木糖 水解 动力学 响应曲面 corncob hydrochloric acid nitric acid xylose hydrolysis kinetics response surface
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参考文献17

  • 1Qu Y, Zhu M, Liu K, et al. Studies on cellulosic etha- nol production for sustainable supply of liquid fuel in China [ J]. Biotechnology Journal, 2006, 1 ( 11 ) : 1 235- 1 240.
  • 2Fang X, Shen Y, Zhao J, et al. Status and prospect of ligneellulosic bioethanol production in China[ J]. Biore- source Technology, 2010, 101(1) :4 814 -4 819.
  • 3Lioyd T A, Wyman C E. Combined sugar yields for di- lute sulfuric acid pretreatment of corn stover followed by enzymatic hydrolysis of the remaining solids [ J ]. Biore- source Technology, 2005, 96 (18) :1 967 - 1 977.
  • 4Cai B, Ge J, Ping W, et a[. Statistical optimization of dilute sulfuric acid pretreatment of corncob for xylose re- covery and ethanol production [ J ]. Biomass and Bioen- ergy, 2012, 36:250-257.
  • 5Cheng K, Wang W, Zhang J, et al. Statistical optimiza- tion of sulfite pretreatment of corncob residues for high concentration ethanol production [ J ]. Bioresource Tech- nology, 2012, 102:3 014 -3 019.
  • 6Garrote G, Dominguez H, Parajo J C. Autohydrolysis ofcorncob : Study of non-isothermal operation for xylopligo- saccharide production [ J ]. Journal of Food Engineering, 2002, 52(3) : 211 -218.
  • 7Zhang R, Lu X, Zhang S, et al. Modeling and optimi- zation of dilute nitric acid hydrolysis on corn stover[ J]. Journal of Chemical Technology and Biotechnology, 2011, 86(2): 306-314.
  • 8Herrera A, Ramirez J A, Vazquez M. Production of xy- lose from sorghum straw using hydrochloric acid [ J ]. Journal of Cereal Science, 2003, 37 (3) : 267 - 274.
  • 9Garrote G, Dominguez H, Parajo J C. Generation of xy- lose solutions from eucalyptus wood by autohydrolysis- posthydrolysis processes : Posthhydrolysis kinetics [ J ]. Bioresource Technology, 2001, 79(2) : 155 -164.
  • 10Rodriguez C A, Ramirez J A, Vazquez M. Hydrolysis of sugarcane bagasse using nitric acid: A kinetic assess- ment[J]. Journal of Food Engineering, 2004, 61: 143 - 152.

二级参考文献12

  • 1罗鹏,刘忠.木质生物资源的水解[J].林产化学与工业,2006,26(2):99-104. 被引量:26
  • 2勇强,徐勇,宋向阳,余世袁.玉米秸秆生物法制取酒精的中间试验[J].纤维素科学与技术,2006,14(3):37-40. 被引量:21
  • 3GRAY K A,ZHAO L S, EMPAGE M. Bioethanol [ J ]. Current Opinion in Chemical Biology. ,2006,10:141-146.
  • 4KIM S, DALE B E. Global potential bioethanol production from wasted crops and crop residues[ J ]. Biomass and Bioenergy,2004 (26) :361- 375.
  • 5KADAM K L, MCMILLIAN J D. Availability of corn stover as a sustainable feedstock for bioethanol production [ J ]. Bioresource Technology, 2003(88) :17-25.
  • 6BAYER E A,LAMED R, HIMMEL M E. The potential of cellulases and cellulosomes for cellulosic waste management [ J ]. Current Opinion in Biotechnology ,2007 ( 18 ) :237-245.
  • 7BADAL C S, ITEN L B, COTTA M A, et al. Dilute acid pretreatment,enzymatic saccharification and fermentation of wheat straw to ethanol[ J ]. Process Biochemistry ,2005,40:3693-3700.
  • 8SLUITER A. Biomass Analysis Technology. Team Laboratory. Analytical Procedure[ M ]. [ S. l. ] :NREL,2005.
  • 9ZHAO H, KWAK J H,ZHAN C, et al. Studying cellulose fiber structure by SEM, XRD, NMR and acid hydrolysis [ J ]. Carbohydrate Polymers, 2007,68:235-241.
  • 10KLINKE H B,THOMSEN A B, AHRING B K. Inhibition of ethanol-producing yeast and bacteria by degradation products produced during pretreatment of biomass[ J]. Appl Microbiol Biotechnot,2004 ,66 : 10-26.

共引文献24

同被引文献73

  • 1孙姝兰,万甡,刘丹,吴明江,张丽萍.玉米芯水溶性多糖的分离纯化和抗凝血活性研究[J].分子科学学报,2006,22(2):131-134. 被引量:8
  • 2孟卓,郑正,杨世关,李继红.木质纤维素原料预处理技术研究近况[J].四川环境,2007,26(4):113-118. 被引量:9
  • 3Gregg D, Saddler J N. Bioconversion of lingocellulosic residue to ethanol: Process flowsheet development [ J]. Biomass and Bioenergy, 1995, 9( 1/5 ) : 287 - 302.
  • 4Janusz S,Jan F. Technology for conversion of lingo- cel- lulosic biomass to ethanol [ J ]. Biomass and Bioenergy, 1996, 10 (5/6): 367-375.
  • 5Bai D, Li S, Liu Z, et al. Enhanced 1-( + )-lactic acid production by an adapted strain of rhizopus oryzae using corncob hydrolysate [ J]. Applied Biochemistry and Bio- technology, 2008, 144( 1 ) : 79 -85.
  • 6Olofsson K, Bertilsson M, Lid6n G. A short review on SSF-An interesting process option for ethanol production from lignocellulosic feedstocks [ J ]. Biotechnology for Biofuels, 2008, 1(7) :1-14.
  • 7Yun C C, Alan B, Michael H P. Analysis of biomass cellulose in simultaneous saccharification and fermenta- tion process [ J]. Applied Biochemistry and Biotechnol- ogy, 1997, 66(3) : 249 -262.
  • 8NREL. Chemical analysis and testing standard proce- dure, No: 001 -014, National Renewable Energy Labs, Golden, CO.
  • 9K6d~tr Z, Szengyel Z, R6czey K. Simultaneous sacchar- ification and fermentation(SSF) of industrial wastes for the production of ethanol [ J ]. Industrial Crops and Products, 2004, 20( 1 ) : 103 - 110.
  • 10Soclerstron J, Galbe M, Zacchi G. Comparison of SHF and SSF of two-step steam pretreated softwood for etha- nol production [ J ]. Journal of Wood Chemistry and Technology, 2005, 25:187-202.

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