脱盐和水回收:膜污染的控制

A. Reddy, D. Mohan, P. R. Buch, S. Joshi, P. Ghosh
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引用次数: 5

摘要

超滤(UF)、纳滤(NF)和反渗透(RO)技术被广泛用于生产安全饮用水,以及从各种工业废水中回收可重复使用的水。在这些过程中,特别是在水回收应用中最常见的现象是膜污染,而膜污染的控制被认为是一个重大的挑战。据报道,具有带电和亲水表面的膜不易受污染,而且通常是可逆的。通过对合适的膜进行表面改性,制备了表面含有负电荷和/或中性亲水性官能团的UF/RO膜。在4 kg/cm²的操作压力下,表面改性膜对Na2SO4的分离率为68% ~ 85%,对MgSO4的分离率为19% ~ 31%,对NaCl的分离率为10% ~ 26%,对CaCl2的分离率为2% ~ 12%,水渗透率为9 ~ 50 l/m²-h。利用超滤膜对含有600-1000 Da分子溶质和无机溶质的活性染料废水进行了水回收试验。将表面改性反渗透膜用于微咸水的脱盐。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Desalination and water recovery: control of membrane fouling
Ultrafiltration (UF), Nanofiltration (NF) and Reverse Osmosis (RO) technologies are widely used for the production of safe drinking water, and for the recovery of reusable water from various industrial effluent streams. The most commonly encountered phenomenon in these processes, especially in water recovery application, is membrane fouling, and control of membrane fouling is regarded as a significant challenge. Membranes with charged and hydrophilic surfaces are reported to be less susceptible to fouling and often reversible. UF/RO membranes containing negatively charged and/or neutral hydrophilic functional groups on the surface were prepared by surface modification of suitable membranes. The surface modified membranes exhibited separations of 68%–85% for Na2SO4, 19%–31% for MgSO4, 10%–26% for NaCl and 2%–12% for CaCl2 with water permeation rates of 9–50 l/m²-h at the operating pressure of 4 kg/cm². The UF membranes were tested for water recovery from reactive dye effluents containing solutes with molecular sizes in the range of 600–1000 Da along with inorganic solutes. Surface-modified RO membranes were utilised for desalination of brackish water.
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