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Pervaporation of methanol/MTBE/C_5 ternary mixtures through the CA membrane

机译:甲醇/ MTBE / C_5三元混合物透过CA膜的全蒸发

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The pervaporation separation properties for the MTBE/C_5/methanol ternary system and three corresponding binary mixtures were measured with a cellulose acetate membrane. It was found that there are very high pervaporation properties for methanol/C_5 (the flux of methanol >430 g/m~2.h). However, the flux of methanol for methanol/MTBE is lower than 90 g/m~2.h. The methanol concentrations in the permeate are similar for the two binary mixtures. From the result of ternary mixtures, the flux of methanol decreased from about 450 to 100 g/m~2.h, with an increase of MTBE concentration in the feed from 5 to 50 wt%, and there is a strong accompany effect between methanol and MTBE. Based on Fick's law and the accompany effect, the models of pervaporation flux and quasi-phase equilibrium of permeate components for the ternary mixture were advanced. The calculated values agreed with the experiment results. The models will be useful for separation process design of the MTBE/C_5/methanol ternary mixture.
机译:用乙酸纤维素膜测量了MTBE / C-5 /甲醇三元体系和三种相应的二元混合物的渗透蒸发分离性能。发现甲醇/ C_5具有非常高的全蒸发性能(甲醇流量> 430 g / m〜2.h)。然而,甲醇对甲醇/ MTBE的通量低于90g / m〜2.h。对于两种二元混合物,渗透液中的甲醇浓度相似。从三元混合物的结果看,甲醇的流量从约450降低至100 g / m〜2.h,进料中MTBE的浓度从5 wt%增加至50 wt%,并且甲醇之间有很强的伴随作用和MTBE。根据菲克定律和伴随效应,建立了三元混合物的渗透汽化通量和渗透组分的准相平衡模型。计算值与实验结果一致。该模型将对MTBE / C_5 /甲醇三元混合物的分离过程设计有用。

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