Separation of Butanol Using Pervaporation: A Review of Mass Transfer Models

H. Azimi, J. Thibault, F. Tezel
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引用次数: 12

Abstract

Pervaporation is a suitable technique for butanol recovery from aqueous solutions especially ABE fermentation broths. The performance of the membrane, in terms of permeation flux and modelling of the mass transfer through membranes provides a deeper understanding, which may assist to orient the research and the development of pervaporation processes. Modelling of the mass transport through the membrane is based on sorption and diffusion of the components into and across the membrane. In this study, an overview of the different models used for the pervaporation separation of butanol is presented. Up to now, the solutiondiffusion based models were the main methods used and the Maxwell-Stefan theory was very limited. In addition, to our knowledge, the pore-flow model was not applied for the modelling of butanol pervaporation separation. Moreover, the Maxwell-Stefan theory seems to be the most accurate mass transfer model to be used for the pervaporation separation method in comparison to the other models.
渗透蒸发分离丁醇:传质模型综述
渗透蒸发是一种适用于从水溶液特别是ABE发酵液中回收丁醇的技术。膜的性能,从渗透通量和膜传质建模方面提供了更深入的理解,这可能有助于定向渗透蒸发过程的研究和发展。通过膜的质量传输的建模是基于组分进入和穿过膜的吸收和扩散。在本研究中,概述了用于丁醇渗透蒸发分离的不同模型。到目前为止,基于溶液扩散的模型是主要的方法,麦克斯韦-斯蒂芬理论非常有限。此外,据我们所知,孔流模型并未应用于丁醇渗透蒸发分离的建模。此外,与其他模型相比,麦克斯韦-斯蒂芬理论似乎是最准确的传质模型,用于渗透蒸发分离方法。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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