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Sodium and potassium removal from brackish water by nanofiltration membrane: single and binary salt mixtures

机译:纳滤膜从微咸水中去除钠和钾:单盐和二元盐混合物

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In this study, the removal efficiency of sodium (Na+) and potassium (K+) by nanofiltration (NF) process was investigated. The experiments was conducted by variation of influent concentration of Na+ and K+, flow rate, solution pH and also co-existing anions and cations. The results showed that with increasing influent concentration of Na+ from 200 to 400 mg/L, the removal efficiency decreased from 68.9% to 63.1% and K+ removal efficiency declined from 89.1% to 83.4% with increasing concentration from 20 to 60 mg/L. As the solution pH was raised from 4 to 9, the Na+ and K+ removal efficiency increased from 66.5% to 74.1% and 87.5% to 93.5% and correspondence with deceasing the concentration of Na+ and K+ in permeate water from 67.1 mg/L to 51.8 mg/L and from 2.51 mg/L to 1.32 mg/L, respectively. In addition, as the flow rate was varied of 0.4 L/min to 0.8 L/min, the Na+ and K+ rejection by NF descended approximately 5%. The most important of effective co-exist anions and cations on Na+ and K+ rejection were nitrate and magnesium, respectively. Consequently, the NF process was recognized as efficient, convenience and low cost method for Na+ and K+ removal from brackish water.
机译:在这项研究中,研究了纳滤(NF)工艺去除钠(Na +)和钾(K +)的效率。通过改变进水Na +和K +的浓度,流速,溶液pH值以及共存的阴离子和阳离子进行实验。结果表明,随着进水Na +浓度从200 mg / L增加到400 mg / L,去除率从68.9%降低到63.1%,K +去除率从89.1%降低到83.4%,浓度从20 mg / L增加到60 mg / L。随着溶液pH值从4增加到9,Na +和K +的去除效率从66.5%上升到74.1%和87.5%上升到93.5%,并且对应于渗透水中Na +和K +的浓度从67.1 mg / L降低到51.8。 mg / L和2.51 mg / L至1.32 mg / L。此外,当流速从0.4 L / min更改为0.8 L / min时,NF对Na +和K +的排斥率下降约5%。在Na +和K +排斥方面,最重要的有效共存阴离子和阳离子分别是硝酸盐和镁。因此,NF工艺被认为是从微咸水中去除Na +和K +的高效,便捷和低成本的方法。

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