Model-Based Analysis for Acetone-Butanol-Ethanol Production Process through a Dynamic Simulation

被引:0
|
作者
Morales-Rodriguez, Ricardo [1 ]
Rodriguez-Gomez, Divanery [2 ]
Sales-Cruz, Mauricio [3 ]
de los Reyes-Heredia, Jose A. [1 ]
Perez Cisneros, Eduardo S. [1 ]
机构
[1] Univ Autonoma Metropolitana Iztapalapa, Dept Ingn Proc & Hidraul, Av San Rafael Atlixco 186, Mexico City 09340, DF, Mexico
[2] Univ Autonoma Metropolitana Iztapalapa, Dept Biotecnol, Mexico City 09340, DF, Mexico
[3] Univ Autonoma Metropolitana Cuajimalpa, Proc & Technol Dept, Mexico City 01120, DF, Mexico
关键词
Acetone-butanol-ethanol production; model-based analysis; dynamic modelling;
D O I
暂无
中图分类号
TP39 [计算机的应用];
学科分类号
081203 ; 0835 ;
摘要
This study presents an analysis for acetone, butanol and ethanol production process. Firstly, a systematic methodology for model-based simulation is proposed in order to perform an appropriate modelling task in the analysis of production processes. The implementation of the systematic methodology allowed the evaluation of four ABE production processes with different operating scenarios such as, continuous and continuous with recycle in the enzymatic hydrolysis and ABE fermentation, relying on a benchmarking criterion (kg-butanol/kg-dry-biomass). The results show that recycle in both sections improve butanol production, but especially when this was present in the enzymatic hydrolysis section. The highest yield was found in the configuration with continuous and recycle mode for enzymatic hydrolysis and ABE fermentation.
引用
收藏
页码:133 / 138
页数:6
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