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Hydrophilic Zeolite Membranes for Pervaporation of Water

机译:亲水性沸石膜,用于普及水

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Abstract: Water was separated from water/2,2,2-trifluoroethyl alcohol (TFEA) mixtures by pervaporation using hydrothermally synthesized NaA and NaY zeolite membranes. The effect of a TFEA feed concentration and a temperature was studied on the permeation flux and the separation factor. The separation factors obtained with the NaA zeolite membrane were found to be 10 times higher than those obtained with the NaY zeolite membrane which were always no less than 1,000 at all experimental conditions. The water flux through the NaY zeolite membrane was observed to be 1.2 times larger than that of the NaA zeolite membrane. The water flux increased significantly with increase of the temperature for both NaA and NaY zeolite membranes. The TFEA flux through NaA zeolite membrane was not much changed by the increase of the temperature when the TFEA concentration was below 0.8 mole fraction in a solution. On the other hand, the TFEA flux through the NaY zeolitemembrane rapidly increased with increase of the temperature at the feed concentration below 0.8 mole fraction of TFEA. Long-term pervaporation tests showed a good stability since the total flux through the NaA zeolite membrane was stabilized at about 1,250g/m 2 hr and the separation factor of 2.5 ×10 5 and total flux of about 1,750g/m 2 hr and the separation factor of about 7 ×10 3 for the NaY zeolite membrane.
机译:摘要:通过使用水热合成的NAA和NAY沸石膜通过渗透蒸发分离水与水/ 2,2,2-三氟乙醇(TFEA)混合物分离。研究了TFEA进料浓度和温度的效果对渗透通量和分离因子研究。发现用NAA沸石膜获得的分离因子比用NY沸石膜获得的10倍,在所有实验条件下始终不小于1,000。通过NAY沸石膜的水通量观察到比NAA沸石膜大的1.2倍。随着NAA和NAY沸石膜的温度的增加,水通量显着增加。通过NAA沸石膜的TFEA通量在溶液中TFEA浓度低于0.8摩尔分数时,通过温度的增加并不多大。另一方面,通过NY Zeolitembrane的TFEA通量随着饲料浓度的升高而迅速增加,饲料浓度低于0.8摩尔分数的TFEA。长期渗透蒸发试验显示出良好的稳定性,因为通过NAA沸石膜的总通量稳定为约1,250g / m 2小时,分离因子为2.5×10 5和约1,750g / m 2小时的总通量和对于NY沸石膜的分离因子约7×10 3。

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