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首页> 外文期刊>Journal of Chemical Engineering of Japan >Pervaporation separation of methanol from methanol-t-amyl methyl ether mixture by polyion complex membrane
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Pervaporation separation of methanol from methanol-t-amyl methyl ether mixture by polyion complex membrane

机译:聚离子络合物膜从甲醇-叔戊基甲基醚混合物中渗透蒸发分离甲醇

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Pervaporation separation of methanol (MeOH) from methanol-t-amyl methyl ether (TAME) mixtures is carried out using polyion complex (PIC) hollow fiber membrane. The sorption experiment is performed to observe the equilibrium relations between solute concentrations in the solution and in the membrane phase. With increasing MeOH weight fraction in the feed solution, the permeation flux of MeOH increases, but that of TAME remains almost constant. Considering the swelling effect by MeOH component, the flux model is described using diffusion coefficients dependent on MeOH concentration in the membrane and it can be successfully fitted to experimental data. The separation factor of MeOH ranges from 12 to 73, and decreases with increasing MeOH weight fraction in the feed solution. [References: 8]
机译:使用聚离子络合物(PIC)中空纤维膜从甲醇-叔戊基甲基醚(TAME)混合物中进行甲醇(MeOH)的全蒸发分离。进行吸附实验以观察溶液和膜相中溶质浓度之间的平衡关系。随着进料溶液中MeOH重量分数的增加,MeOH的渗透通量增加,但TAME的渗透通量几乎保持恒定。考虑到MeOH组分的溶胀作用,使用取决于膜中MeOH浓度的扩散系数描述了通量模型,该通量模型可以成功地拟合到实验数据中。 MeOH的分离系数范围为12到73,并且随着进料溶液中MeOH重量分数的增加而降低。 [参考:8]

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