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Separation of Cr(VI) by zeolite-clay composite membranes modified by reaction with NO_x

机译:与NO_x反应改性的沸石-粘土复合膜分离Cr(VI)

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摘要

In this work,we report the use of modified zeolite-clay composite ultrafiltration membranes (preparation of the unmodified (Z_1),the nitrated (Z_2,modified using NO_x) and the aminated (Z_3) membrane have been described in our earher publication [1]) for the separation of chromic acid solution.Experiments show that the observed rejection coefficients of the membranes increase on modification from approx 20% for Z_1 to approx 40% for Z_2 and approx 50% for Z_3 membrane.Experimental data is analyzed using the irreversible thermodynamic approach (Spiegler-Kedem equations) [2].The study shows that the chemical modification of membranes leads to a rise in the intrinsic rejection (highest R approx 50% for Z_1 to approx 60% for Z_2 and approx 66% for Z_3 membrane) coefficients.It is also found that while the observed rejection show anomalous trend with variation in pressure while the intrinsic rejection increases with increase in pressure,a trend typical of the separation of electrolyte through charged membranes.
机译:在这项工作中,我们报道了在我们较早的出版物中已经描述了使用改性沸石-粘土复合超滤膜(未改性(Z_1)的制备,硝化(Z_2,使用NO_x改性)和胺化(Z_3)膜的使用[1]。实验表明,观察到的膜的截留系数在改性时从Z_1的约20%增至Z_2的约40%和Z_3膜的约50%增大。使用不可逆分析法分析实验数据热力学方法(Spiegler-Kedem方程)[2]。研究表明,膜的化学改性导致固有排斥性增加(Z_1的最高R值约为50%,Z_2的最高R值约为60%,Z_3膜的最高R值约为66%。还发现,虽然观察到的排阻表现出随压力变化的异常趋势,而固有排阻随着压力的增加而增加,但这种趋势是电解液通过gh带电的膜。

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