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Pervaporation membrane bioreactor with permeate fractional condensation and mechanical vapor compression for energy efficient ethanol production

机译:具有渗透物部分冷凝和机械蒸汽压缩功能的全蒸发膜生物反应器,可高效生产乙醇

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摘要

Improved process separation factor and heat integration are two key issues to increase the energy efficiency of ethanol production in a pervaporation membrane bioreactor (PVMBR). A PVMBR with permeate fractional condensation and mechanical vapor compression was developed for energy efficient ethanol production. A condensation model based on the mass balance and thermodynamic equilibrium in the partial vacuum condenser was developed for predicting the purification performance of the permeate vapor. Three runs of ethanol fermentation-pervaporation experiment were carried out and ethanol concentration of higher than 50 wt% could be achieved in the final condensate, with the separation factor of the process for ethanol increased to 20. Ethanol production could be enhanced in the bioreactor and 17.1 MJ of the energy could be produced in per liter of fermentation broth, owing to 27.0 MJ/kg heating value of the recovered ethanol. Compared with the traditional pervaporation process with low temperature condensation for ethanol production, 50% of the energy would be saved in the process. The energy consumption would be further reduced, if the available energy of the permeate vapor was utilized by integrating the mechanical vapor compression heat pump. (C) 2016 Elsevier Ltd. All rights reserved.
机译:改进的工艺分离因子和热集成度是提高全蒸发膜生物反应器(PVMBR)中乙醇生产的能源效率的两个关键问题。开发了具有渗透物部分冷凝和机械蒸汽压缩功能的PVMBR,用于高效节能的乙醇生产。建立了基于质量平衡和部分真空冷凝器热力学平衡的冷凝模型,用于预测渗透蒸汽的净化性能。进行了三步乙醇发酵-全蒸发实验,最终冷凝物中的乙醇浓度可达到50 wt%以上,而乙醇工艺的分离因子增加到20。在生物反应器中可以提高乙醇产量。每升发酵液可产生17.1兆焦耳的能量,这是因为回收的乙醇的热值为27.0兆焦耳/千克。与传统的低温冷凝法全蒸发工艺生产乙醇相比,该工艺可节省50%的能量。如果通过集成机械蒸汽压缩热泵来利用渗透蒸汽的可用能量,则能量消耗将进一步降低。 (C)2016 Elsevier Ltd.保留所有权利。

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