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Pervaporation performance analysis and prediction - using a hybrid solution-diffusion and pore-flow model

机译:全蒸发性能分析和预测-使用混合溶液-扩散和孔流模型

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A hybrid mathematic model for pervaporation is proposed which incorporates the concepts of solution-diffusion model and pore model. The model allows performance prediction as well as the establishment of the internal concentration and pressure profiles within the membrane. The model parameters specific to the particular membrane and mixture system are determined using liquid sorption and pervaporation experimental data. The model is experimentally examined using ethanol-water mixtures and poly(dimethyl siloxane)-poly(vinyldiene fluoride) (PDMS-PVDF) composite membranes. The characteristics of flux and separation factor predicted using the model are in fair agreement with the experimental data under various feed concentrations and downstream pressures for different membrane arrangements, including single-layer, reverse single-layer and double-layer PDMS-PVDF composite membranes. Internal profiles of pressure, concentration and component mole fraction can be established using the model. Concentration polarization phenomena for ethanol and water are located at membrane interfaces and vapor-liquid interfaces, respectively. Performances of several different membrane designs are compared using the model. (c) 2007 Taiwan Institute of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
机译:提出了一种混合蒸发的数学模型,该模型结合了溶液扩散模型和孔隙模型的概念。该模型可以预测性能,并在膜内建立内部浓度和压力曲线。使用液体吸附和全蒸发实验数据确定特定膜和混合物系统特有的模型参数。使用乙醇-水混合物和聚(二甲基硅氧烷)-聚(乙烯基二氟乙烯)(PDMS-PVDF)复合膜对模型进行实验检验。使用该模型预测的通量和分离因子的特性与在各种进料浓度和下游压力下针对不同膜布置(包括单层,反向单层和双层PDMS-PVDF复合膜)的实验数据完全吻合。可以使用该模型建立压力,浓度和组分摩尔分数的内部曲线。乙醇和水的浓度极化现象分别位于膜界面和气液界面。使用该模型比较了几种不同膜设计的性能。 (c)2007年台湾化学工程师学会。由Elsevier B.V.发布。保留所有权利。

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