A process for energy-efficient high-solids fed-batch enzymatic liquefaction of cellulosic biomass

被引:23
|
作者
Cardona, M. J. [1 ]
Tozzi, E. J. [2 ]
Karuna, N. [3 ]
Jeoh, T. [3 ]
Powell, R. L. [1 ,4 ]
McCarthy, M. J. [3 ,4 ]
机构
[1] Univ Calif Davis, Dept Chem Engn & Mat Sci, Davis, CA 95616 USA
[2] Aspect Imaging, Davis, CA 95616 USA
[3] Univ Calif Davis, Dept Biol & Agr Engn, Davis, CA 95616 USA
[4] Univ Calif Davis, Dept Food Sci & Technol, Davis, CA 95616 USA
基金
美国食品与农业研究所;
关键词
Fed-batch; Enzymatic hydrolysis; Liquefaction; Rheology; Magnetic resonance imaging; LIGNOCELLULOSIC ETHANOL-PRODUCTION; PRETREATED CORN STOVER; YIELD-STRESS; SIMULTANEOUS SACCHARIFICATION; WHEAT-STRAW; HYDROLYSIS; VISCOSITY; FERMENTATION; LOADINGS;
D O I
10.1016/j.biortech.2015.09.042
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
The enzymatic hydrolysis of cellulosic biomass is a key step in the biochemical production of fuels and chemicals. Economically feasible large-scale implementation of the process requires operation at high solids loadings, i.e., biomass concentrations >15% (w/w). At increasing solids loadings, however, biomass forms a high viscosity slurry that becomes increasingly challenging to mix and severely mass transfer limited, which limits further addition of solids. To overcome these limitations, we developed a fed-batch process controlled by the yield stress and its changes during liquefaction of the reaction mixture. The process control relies on an in-line, non-invasive magnetic resonance imaging (MRI) rheometer to monitor real-time evolution of yield stress during liquefaction. Additionally, we demonstrate that timing of enzyme addition relative to biomass addition influences process efficiency, and the upper limit of solids loading is ultimately limited by end-product inhibition as soluble glucose and cellobiose accumulate in the liquid phase. (C) 2015 Elsevier Ltd. All rights reserved.
引用
收藏
页码:488 / 496
页数:9
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