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A hybrid ion exchange-nanofiltration (HIX-NF) process for energy efficient desalination of brackish/seawater

机译:混合离子交换-纳滤(HIX-NF)工艺用于微咸水/海水的高能效脱盐

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摘要

This study reports a new hybrid ion exchange-nanofiitration (HIX-NF) process for desalination of sea and brackish water that can attain significant energy economy over the conventional membrane-based pressure driven processes. In this hybrid process, an ion exchange step converts monovalent chlcride ions of saline water to divalent sulfate ions and the resulting solution, having a reduced osmotic pressure than the feed, is desalinated using a nanofiltration (NF) membrane. The sulfate rich reject stream from the NF process is used to regenerate the anion exchanger. Results validate that NF membranes can desalinate sodium sulfate solution at a much lower transmembrane pressure compared to RO membranes as well as yield a higher permeate flux. The sulfate-chloride selectivity of the anion exchangers plays important role in sustainability of the process. Laboratory studies have revealed that a single type of anion exchanger cannot sustain the process for saline water with different salt concentrations. However, anion exchangers with different sizes of amine functional groups (e.g. quaternary-, tertiary-, secondary- and primary amine) hold the promise that the process can be tailored to achieve sustainability. Laboratory studies have validated the basic premise of the hybrid process including greater than two times less energy requirement than RO process for the same feed water and same permeate recovery condition.
机译:这项研究报告了一种用于海水和微咸水脱盐的新型混合离子交换-纳米过滤(HIX-NF)工艺,与传统的基于膜的压力驱动工艺相比,该工艺可实现显着的能源经济性。在该混合过程中,离子交换步骤将盐水的一价氯离子转化为二价硫酸根离子,并使用纳滤(NF)膜对所得溶液的渗透压比进料降低。来自NF工艺的富含硫酸盐的废料流用于再生阴离子交换剂。结果证实,与RO膜相比,NF膜可以在低得多的跨膜压力下使硫酸钠溶液脱盐,并产生更高的渗透通量。阴离子交换剂的硫酸盐-氯化物选择性在该方法的可持续性中起重要作用。实验室研究表明,对于不同盐浓度的盐水,单一类型的阴离子交换剂无法维持该过程。但是,具有不同尺寸的胺官能团(例如季胺,叔胺,仲胺和伯胺)的阴离子交换剂有望实现该工艺,以实现可持续性。实验室研究已经验证了混合工艺的基本前提,包括对于相同的给水和相同的渗透物回收条件,其能量需求比反渗透工艺少两倍以上。

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