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Scaling of nanofiltration membranes used for chromium(III) ions recovery from salt solutions

机译:用于铬(III)离子从盐溶液中恢复的纳米滤膜的缩放

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The effect of membranes' structure on the efficiency of chromium(III) ions recovery from salt solution at low pH and the efficiency of chemical cleaning of these membranes were analyzed in this work. The nanofiltration membranes (DL and HL) used in this study were provided by GE Osmonics. The DL membrane had an irregular, dense support layer structure, while the HL membrane had a loose one. In the case of the DL membrane, it was found that, under tested solutions, the layer of mineral scale formed on the surface gradually decreases the membrane permeability coefficient. In the case of the DL membrane, the scaling was observed only on the surface. On the other hand, a small roughness (118 angstrom) and low density charge (zeta potential at level -4) of the HL membrane causes an uneven growth in deposits and, consequently, irregular nature of the surface structure which hinders the removal of accumulated sediment from the tested membranes' surface. Additionally, the loose structure of the support layer of HL membrane contributes to its internal scaling. Consequently, the permanently loose structure of the HL membrane permeability coefficient was observed.
机译:在该工作中分析了膜对从盐溶液中回收铬(III)离子的效率的影响及其对这些膜的化学清洁效率。本研究中使用的纳滤膜(DL和HL)由Ge锇提供。 DL膜具有不规则,致密的支撑层结构,而HL膜具有松散的胶囊。在DL膜的情况下,发现,在测试的溶液下,在表面上形成的矿物垢层逐渐降低膜渗透系数。在DL膜的情况下,仅在表面上观察到缩放。另一方面,HL膜的小粗糙度(118埃)和低密度电荷(Zeta电位为-4)导致沉积物的增长不均匀,因此妨碍了累积的表面结构的不规则性质从测试的膜表面沉积物。另外,HL膜的支撑层的松散结构有助于其内部缩放。因此,观察到HL膜渗透系数的永久性松散的结构。

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