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用于 N-甲基-2-吡咯烷酮/水混合物渗透蒸发的耐溶剂壳聚糖/聚(醚嵌段酰胺)复合膜。

Solvent resistant chitosan/poly(ether-block-amide) composite membranes for pervaporation of n-methyl-2-pyrrolidone/water mixtures.

机构信息

Membrane Separations Group, Chemical Engineering Division, Indian Institute of Chemical Technology, Hyderabad 500007, India.

Process Simulation and Control Group, Chemical Engineering Division, Indian Institute of Chemical Technology, Hyderabad 500007, India.

出版信息

Carbohydr Polym. 2016 Jan 20;136:1170-81. doi: 10.1016/j.carbpol.2015.10.037. Epub 2015 Oct 22.

Abstract

A novel composite barrier comprising of hydrophilic and solvent resistant chitosan (CS) membrane on porous solvent resistant poly(ether-block-amide) (PEBA-2533) substrate was synthesized for pervaporation (PV) based dehydration of the polar aprotic n-methyl-2-pyrolidone (NMP) green solvent. The composite barrier was crosslinked with tetraethyl orthosilicate (TEOS) to control swelling and enhance selectivity. Operating parameters such as feed water concentration, permeate pressure and membrane thickness were varied to assess membrane flux and selectivity. A two-dimensional finite element method (FEM) model was developed to predict the concentration profile within the membrane through computational fluid dynamics (CFD). On the basis of complete mixing experiments, a numerical simulation was performed to predict membrane area requirement and exit streams' compositions for commercial pervaporation units operated in plug flow mode. Both unmodified chitosan and tetraethyl orthosilicate crosslinked composite membranes successfully separated feed mixture containing 4.6 wt% water by exhibiting water fluxes of 0.024 and 0.019 kg/m(2)h, whereas the corresponding selectivities were found to be as high as 182 and 225, respectively.

摘要

一种新型复合阻隔层由亲水性和耐溶剂性壳聚糖(CS)膜和多孔耐溶剂性聚(醚-嵌段-酰胺)(PEBA-2533)基底组成,用于极性非质子 N-甲基-2-吡咯烷酮(NMP)绿色溶剂的渗透蒸发(PV)脱水。复合阻隔层用四乙氧基硅烷(TEOS)交联,以控制溶胀和提高选择性。改变操作参数,如进料浓度、渗透压力和膜厚度,以评估膜通量和选择性。通过计算流体动力学(CFD)开发了二维有限元方法(FEM)模型,以预测膜内的浓度分布。根据完全混合实验,进行了数值模拟,以预测在塞流模式下运行的商业渗透蒸发装置的膜面积需求和出口料流的组成。未经修饰的壳聚糖和四乙氧基硅烷交联复合膜都成功地分离了含有 4.6wt%水的进料混合物,水通量分别为 0.024 和 0.019kg/m(2)h,相应的选择性高达 182 和 225。

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