Kinetics of glucose decomposition during dilute-acid hydrolysis of lignocellulosic biomass

被引:131
|
作者
Qian Xiang
Yong Y. Lee
Robert W. Torget
机构
[1] Auburn University,Department of Chemical Engineering
[2] National Renewable Energy Laboratory,National BioEnergy Center
关键词
Reaction kinetics; glucose decomposition; dilute acid hydrolysis; kinetic modeling; acid-soluble lignin; acid-base catalysis rules;
D O I
10.1385/ABAB:115:1-3:1127
中图分类号
学科分类号
摘要
Recent research work in-house both at Auburn University and National Renewable Energy Laboratory has demonstrated that extremely low concentrations of acid (e.g., 0.05–0.2 wt% sulfuric acid) and high temperatures (e.g., 200–230°C) are reaction conditions that can be effectively applied for hydrolysis of the cellulosic component of biomass. These conditions are far from those of the conventional dilute-acid hydrolysis processes, and the kinetic data for glucose decomposition are not currently available. We investigated the kinetics of glucose decomposition covering pH values of 1.5–2.2 and temperatures of 180–230°C using glass ampoule reactors. The primary factors controlling glucose decomposition are the reaction medium, acid concentration, and temperature. Based on the experimental data, a kinetic model was developed and the best-fit kinetic parameters were determined. However, a consistent discrepancy in the rate of glucose disappearance was found between that of the model based on pure glucose data and that observed during the actual process of lignocellulosic biomass hydrolysis. This was taken as an indication that glucose recombines with acid-soluble lignin during the hydrolysis process, and this conclusion was incorporated accordingly into the overall model of glucose decomposition.
引用
收藏
页码:1127 / 1138
页数:11
相关论文
共 50 条
  • [21] Conversion of rice straw to sugars by dilute-acid hydrolysis
    Karimi, K
    Kheradmandinia, S
    Taherzadeh, MJ
    [J]. BIOMASS & BIOENERGY, 2006, 30 (03): : 247 - 253
  • [22] Dilute-acid hydrolysis of sugarcane bagasse at varying conditions
    Markus Neureiter
    Herbert Danner
    Christiane Thomasser
    Bamusi Saidi
    Rudolf Braun
    [J]. Applied Biochemistry and Biotechnology, 2002, 98-100 : 49 - 58
  • [23] A comprehensive kinetic model for dilute-acid hydrolysis of cellulose
    Xiang, Q
    Kim, JS
    Lee, YY
    [J]. APPLIED BIOCHEMISTRY AND BIOTECHNOLOGY, 2003, 105 : 337 - 352
  • [24] Dilute-acid hydrolysis of sugarcane bagasse at varying conditions
    Neureiter, M
    Danner, H
    Thomasser, C
    Saidi, B
    Braun, R
    [J]. APPLIED BIOCHEMISTRY AND BIOTECHNOLOGY, 2002, 98 (1-9) : 49 - 58
  • [25] Modeling sucrose hydrolysis in dilute sulfuric acid solutions at pretreatment conditions for lignocellulosic biomass
    Bower, Shane
    Wickramasinghe, Ranil
    Nagle, Nicholas J.
    Schell, Daniel J.
    [J]. BIORESOURCE TECHNOLOGY, 2008, 99 (15) : 7354 - 7362
  • [26] Strain Construction for Ethanol Production from Dilute-Acid Lignocellulosic Hydrolysate
    Fei Yan
    Fali Bai
    Shen Tian
    Jinxin Zhang
    Zuoyang Zhang
    Xiushan Yang
    [J]. Applied Biochemistry and Biotechnology, 2009, 157 : 473 - 482
  • [27] Shrinking-bed model for percolation process applied to dilute-acid pretreatment/hydrolysis of cellulosic biomass
    Rongfu Chen
    Zhangwen Wu
    Y. Y. Lee
    [J]. Applied Biochemistry and Biotechnology, 1998, 70-72 : 37 - 49
  • [28] A process economic approach to develop a dilute-acid cellulose hydrolysis process to produce ethanol from biomass
    Nick Nagle
    Kelly Ibsen
    Edward Jennings
    [J]. Applied Biochemistry and Biotechnology, 1999, 79 (1-3) : 595 - 607
  • [29] OPTIMIZATION STUDY OF CITRUS WASTES SACCHARIFICATION BY DILUTE-ACID HYDROLYSIS
    Talebnia, Farid
    Pourbafrani, Mohammad
    Lundin, Magnus
    Taherzadeh, Mohammad J.
    [J]. BIORESOURCES, 2008, 3 (01): : 108 - 122
  • [30] Optimization study of citrus wastes saccharification by dilute-acid hydrolysis
    School of Engineering, University of Borås, 501 90 Borås, Sweden
    不详
    [J]. BioResour., 2008, 1 (108-122):