Kinetic modeling for enzymatic hydrolysis of pretreated sugarcane straw

被引:28
作者
Angarita, J. D. [1 ]
Souza, R. B. A. [2 ]
Cruz, A. J. G. [2 ]
Biscaia, E. C., Jr. [1 ]
Secchi, A. R. [1 ]
机构
[1] Univ Fed Rio de Janeiro, Ctr Tecnol, COPPE, Chem Engn Program, BR-21941972 Rio de Janeiro, RJ, Brazil
[2] Univ Fed Sao Carlos, Chem Engn Grad Program, BR-13565905 Sao Carlos, SP, Brazil
关键词
Enzyme biocatalysis; Adsorption; Biokinetics; Modelling; Cellulose; Sugarcane straw; SIMULTANEOUS SACCHARIFICATION; CELLULOSE HYDROLYSIS; MATHEMATICAL-MODEL; ETHANOL-PRODUCTION; LIGNOCELLULOSE; FERMENTATION; PERSPECTIVES; VALIDATION; BIOETHANOL; REACTOR;
D O I
10.1016/j.bej.2015.05.021
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
A semimechanistic multi-reaction kinetic model was developed for modeling enzymatic hydrolysis of pretreated sugarcane straw (SCS) at high-solids concentration. The model, including: enzyme adsorption, xylose formation, end-product inhibition and substrate reactivity, was adjusted from a reference condition (enzyme concentration of 10 FPU/g-cellulose and solid loading of 15% w/v, dry basis). A simplified model was also proposed to overcome high parameter correlation and improve model fidelity. Predictive capacity of both simplified and original model was verified for different enzyme concentration (5-60 FPU/g-cellulose), solids loading (10 and 20%) and end-product sugar inhibition (30 and 60 g/L glucose, 10 g/L cellobiose and 10 g/L xylose). The glucose concentration was predicted with reasonable accuracy by the simplified model, even under critical conditions of sugar-inhibition. The model is able to describe batch saccharification of pretreated SCS at high-solids concentrations. (C) 2015 Elsevier B.V. All rights reserved.
引用
收藏
页码:10 / 19
页数:10
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