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首页> 外文期刊>Separation and Purification Technology >Dehydration of ethylene glycol by pervaporation using poly(N,N-dimethylaminoethyl methacrylate)/polysulfone composite membranes
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Dehydration of ethylene glycol by pervaporation using poly(N,N-dimethylaminoethyl methacrylate)/polysulfone composite membranes

机译:聚(N,N-二甲基氨基乙基甲基丙烯酸甲酯)/聚砜复合膜通过全蒸发进行乙二醇脱水

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摘要

Dehydration of ethylene glycol by pervaporation was carried out using poly(N,N-dimethylaminoethyl methacrylate)/polysulfone (PDMAEMA/PSF) composite membranes prepared by solid/liquid interfacial crosslinking. The effects of feed water concentration and operating temperature on the pervaporation performance were investigated. The membrane performance compared favorably with other membranes reported in literature. At a feed water concentration of 1 mol%, a permeation flux of ~1 mol/(m~2 h) and a permeate water concentration of 99.7 mol% were achieved at 30 °C. The permeation flux was shown to increase with an increase in temperature, while the membrane selectivity was essentially the same. The increase in permeation flux with temperature was primarily due to the increased driving force for permeation, and the membrane permeability was shown to decrease as the temperature increased. The sorption uptake of the permeant in the PDMAEMA membrane was also studied, and it was revealed that the selective permeation of water through the membranes was derived from the diffusion selectivity.
机译:使用通过固/液界面交联制备的聚(N,N-甲基丙烯酸二甲基氨基乙酯)/聚砜(PDMAEMA / PSF)复合膜,通过全蒸发进行乙二醇脱水。研究了给水浓度和操作温度对全蒸发性能的影响。该膜的性能优于文献报道的其他膜。在进水浓度为1 mol%的情况下,在30°C下的渗透通量为〜1 mol /(m〜2 h),渗透水的浓度为99.7 mol%。渗透通量显示出随着温度的升高而增加,而膜的选择性基本相同。渗透通量随温度的增加主要是由于渗透驱动力的增加,并且膜的渗透性随温度升高而降低。还研究了PDMAEMA膜中渗透物的吸附吸收,并且揭示了水通过膜的选择性渗透是由扩散选择性引起的。

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