Concentration of sodium chloride solutions in the processing of concentrates for reverse osmotic water desalification

Mykola Gomelya, Yana Kryzhanovska
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Abstract

The paper examines the processes of concentrating sodium chloride solutions by the electrodialysis method. Given the shortage of reagents and their high prices, this electrodialysis method can be implemented to obtain acid and alkali from solutions of sodium sulfate, alkali, aluminum and iron coagulants. Today, the technologies that, as a result of the process, allow us to obtain valuable materials, substances, products, coagulants as a secondary product, are very justified, economically feasible and, most importantly, allow us to successfully implement the principles of low-waste production. The essence of the process is the use of sodium chloride solutions, which are formed during the desalination of water by reverse osmosis in the form of concentrates. The concentration process was implemented in a three-chamber electrolyzer, in the cathode, anode and working areas, a sodium chloride solution with a concentration of 360 mmol/dm3 was placed. An alkali solution with a concentration of 480 mg-eq/dm3 was used in the anode area. During electrolysis, alkali was formed in the cathode area, due to the diffusion of sodium in the working area and the cathodic reduction of water. Chlorides from the working area moved to the anode area. Hydroxide anions on the anode were oxidized to oxygen, chlorides with sodium formed sodium chloride, the concentration of which increased to 660 mg-eq/dm3. Alkalinity decreased to 68-70 mg-eq/dm3. When changing cathodes and anodes, the process was repeated in some places until the alkalinity in the cathode zone and the concentration of chlorides in the anode zone increased. . A solution of sodium chloride with a concentration of 360 mmol/dm3 was added to the working area where water desalination took place. After nine cycles of electrolysis, a sodium chloride solution with a concentration of 100-150 g/dm3 was obtained. The residual content of sodium chloride in desalinated water reached 50-100 mg/dm3. Sodium chloride solutions with a concentration of 4 to 30 g/dm3 can be used for concentration. It should be noted that after conducting nine cycles of the experiment, we can state that the process of concentration by this electrodialysis method does not lead to an increase in system resistance and energy consumption.
反渗透脱盐浓缩液处理中氯化钠溶液的浓度
研究了电渗析法浓缩氯化钠溶液的工艺过程。由于试剂短缺且价格昂贵,可采用电渗析法从硫酸钠、碱、铝、铁等混凝剂溶液中提取酸、碱。今天,作为这一过程的结果,技术使我们能够获得有价值的材料、物质、产品、混凝剂作为二级产品,这是非常合理的,经济上可行的,最重要的是,使我们能够成功地实施低废物生产的原则。该工艺的本质是使用氯化钠溶液,氯化钠溶液是在反渗透脱盐过程中以浓缩液的形式形成的。浓缩过程在三室电解槽中进行,阴极、阳极和工作区分别放置浓度为360 mmol/dm3的氯化钠溶液。阳极区使用浓度为480 mg-eq/dm3的碱溶液。电解过程中,由于钠在工作区的扩散和水的阴极还原,在阴极区形成碱。氯化物从工作区域移动到阳极区域。阳极上的氢氧根阴离子被氧化成氧,氯化物与钠形成氯化钠,其浓度增加到660 mg-eq/dm3。碱度降至68-70 mg-eq/dm3。当更换阴极和阳极时,在某些地方重复该过程,直到阴极区的碱度和阳极区的氯化物浓度增加。将浓度为360 mmol/dm3的氯化钠溶液加入到海水淡化的工作区域。电解9次后,得到浓度为100-150 g/dm3的氯化钠溶液。淡化水中氯化钠残留量达50 ~ 100 mg/dm3。可采用浓度为4 ~ 30g /dm3的氯化钠溶液进行浓缩。需要说明的是,在进行了9个循环实验后,我们可以说,这种电渗析方法的浓缩过程不会导致系统阻力和能量消耗的增加。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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