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Hollow fiber modules with ceramic-supported PDMS composite membranes for pervaporation recovery of bio-butanol

机译:具有陶瓷支撑PDMS复合膜的中空纤维模块,用于生物丁醇的全蒸发回收

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摘要

The practical application of hollow fiber membranes for pervaporation technology has been received growing attention in recent years. This work reports the development of hollow fiber modules of ceramic-supported polydimethylsiloxane (PDMS) composite membranes applied for pervaporation process. Computational fluid dynamics (CFD) technique was used to simulate and optimize the flow field distribution in the modules with different packing density and cross-section layout. The hollow fiber modules with proposed configurations were fabricated in our lab and evaluated by pervaporation measurement in model butanol aqueous solution and real fermentation broth. The results suggested that the design of packing density and cross-section layout could realize the optimization of module configuration. The optimized module filled with 7 bundles of hollow fiber membranes at a high packing density of 560 m(2)/m(3) exhibits a high and stable performance in the real ABE fermentation broth during 120 h continuous operation at 40 degrees C. The average total flux was 1000 g/m(2) h and separation factor were 6.4 for ethanol, 22.2 for butanol and 28.6 for acetone, respectively. Our results demonstrated that the hollow fiber modules developed in this work could be competitive candidates for the practical application in pervaporation recovery of bio-butanol. (C) 2015 Elsevier B.V. All rights reserved.
机译:近年来,中空纤维膜在全蒸发技术中的实际应用受到越来越多的关注。这项工作报告了用于全蒸发过程的陶瓷支撑的聚二甲基硅氧烷(PDMS)复合膜中空纤维组件的开发。计算流体动力学(CFD)技术用于模拟和优化具有不同填充密度和横截面布局的模块中的流场分布。具有建议结构的中空纤维组件是在我们的实验室中制造的,并通过在丁醇水溶液和实际发酵液中的全蒸发测量进行评估。结果表明,通过设计填充密度和横截面布局可以实现模块结构的优化。经过优化的模块以560 m(2)/ m(3)的高堆积密度填充了7束中空纤维膜束,在40°C下连续运行120 h的过程中,在真实的ABE发酵液中显示出高而稳定的性能。平均总通量为1000 g / m(2)h,分离系数分别为:乙醇6.4,丁醇22.2和丙酮28.6。我们的结果表明,在这项工作中开发的中空纤维组件可能是生物丁醇全蒸发回收中实际应用的竞争候选者。 (C)2015 Elsevier B.V.保留所有权利。

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