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Energy, exergy and techno-economic analysis for biobutanol production: a multi-objective optimization approach based on economic and environmental criteria

机译:生物丁醇生产的能源,火用和技术经济分析:基于经济和环境标准的多目标优化方法

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摘要

Currently, butanol obtained by fermentation is considered as potential biofuel. In this work, it has been simulated and optimized a process to produce acetone, butanol and ethanol by means of lignocellulosic material. To accomplish this task, initially, it was planned the raw material selection, followed by the simulation in MATLAB of simultaneous saccharification, fermentation and separation reactor (SFS) and finally, the stream coming from fermentation was purified. The separation stage was selected from three different options to purify that effluent. The entire process was evaluated under a robust optimization process considering environmental, economic and energetic objective functions by means of a hybrid stochastic method, differential evolution with tabu list. The obtained results showed that the best scheme to produce and purify butanol was the SFS-3C, which considers thermally coupled columns to purify acetone, butanol and ethanol. In general terms, it was obtained as result 0.138 $/kg~(butanol), 0.132 points/kg~(butanol)and 66.8 regarding to the total annual cost, environmental impact and exergy efficiency, respectively.
机译:当前,通过发酵获得的丁醇被认为是潜在的生物燃料。在这项工作中,已经模拟并优化了通过木质纤维素材料生产丙酮,丁醇和乙醇的工艺。为了完成此任务,首先计划了原料选择,然后在MATLAB中模拟了同时糖化,发酵和分离反应器(SFS),最后对来自发酵的物流进行了纯化。从三个不同的选项中选择分离阶段以净化该废水。整个过程是在考虑环境,经济和精力充沛的目标函数的强大优化过程下,通过混合随机方法,带有禁忌表的差分进化方法进行评估的。获得的结果表明,生产和纯化丁醇的最佳方案是SFS-3C,它考虑了使用热偶合柱纯化丙酮,丁醇和乙醇的方法。一般而言,就总年度成本,环境影响和火用效率而言,分别获得0.138美元/千克丁醇,0.132点/千克丁醇和66.8的结果。

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