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Energy efficient of ethanol recovery in pervaporation membrane bioreactor with mechanical vapor compression eliminating the cold traps

机译:机械蒸发压缩消除了冷阱的全蒸发膜生物反应器中乙醇的能量回收

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An energy efficient pervaporation membrane bioreactor with mechanical vapor compression was developed for ethanol recovery during the process of fermentation coupled with pervaporation. Part of the permeate vapor at the membrane downstream under the vacuum condition was condensed by running water at the first condenser and the non-condensed vapor enriched with ethanol was compressed to the atmospheric pressure and pumped into the second condenser, where the vapor was easily condensed into a liquid by air. Three runs of fermentation-pervaporation experiment have been carried out lasting for 192 h, 264 h and 360 h respectively. Complete vapor recovery validated the novel pervaporation membrane bioreactor. The total flux of the polydimethylsiloxane (PDMS) membrane was in the range of 350 g m(-2) h(-1) and 600 g m(-2) h(-1). Compared with the traditional cold traps condensation, mechanical vapor compression behaved a dominant energy saving feature. (C) 2016 Elsevier Ltd. All rights reserved.
机译:开发了一种具有机械蒸气压缩功能的高能效全蒸发膜生物反应器,用于在发酵过程中结合全蒸发进行乙醇回收。在真空条件下,膜下游的部分渗透蒸汽在第一冷凝器中通过自来水进行冷凝,富含乙醇的未冷凝蒸汽被压缩至大气压,然后泵入第二冷凝器,该蒸汽易于冷凝通过空气变成液体。进行了三个发酵-全蒸发实验,分别持续了192 h,264 h和360 h。完全的蒸汽回收验证了新型的全蒸发膜生物反应器。聚二甲基硅氧烷(PDMS)膜的总通量在350 g m(-2)h(-1)和600 g m(-2)h(-1)的范围内。与传统的冷阱凝结相比,机械蒸汽压缩表现出主要的节能特征。 (C)2016 Elsevier Ltd.保留所有权利。

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