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Butanol recovery from model solution/fermentation broth by pervaporation: evaluation of membrane performance

机译:通过全蒸发从模型溶液/发酵液中回收丁醇:评估膜性能

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This is an overview of butanol separation from model solutions and fermentation broth by pervaporation. It is difficult to compare different authors' work on butanol separation because of the number of variables involved. These variables include type of membrane, membrane thickness, feed temperature, condensation temperature, vacuum or sweep gas, feed butanol concentration, etc. For comparison we have calculated the butanol concentration in the permeate and butanol flux from the data given by various authors. Polytetrafluoroethylene (PTFE) membrane and polypropylene (PP) membrane pass a large amount of water through the membrane. Fermentation broth was found to decrease flux and selectivity of a liquid membrane. A silicalite membrane offers high butanol flux and high butanol concentration when using fermentation broth. A thin polydimethylsiloxane (PKMS) membrane offers high flux and low selectivity, while a thick memebrane offers high selectivity and low flux.
机译:这是通过全蒸发从模型溶液和发酵液中丁醇分离的概述。由于涉及变量的数量,很难比较不同作者在丁醇分离方面的工作。这些变量包括膜的类型,膜厚度,进料温度,冷凝温度,真空或吹扫气,进料丁醇浓度等。为进行比较,我们根据不同作者提供的数据计算了渗透液中的丁醇浓度和丁醇通量。聚四氟乙烯(PTFE)膜和聚丙烯(PP)膜使大量水通过该膜。发现发酵液降低了液膜的通量和选择性。使用发酵液时,硅沸石膜可提供高丁醇通量和高丁醇浓度。薄的聚二甲基硅氧烷(PKMS)膜提供高通量和低选择性,而厚膜则提供高选择性和低通量。

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