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A Novel Brine Precipitation Process with the Aim of Higher Permeate Water Recovery

机译:以高渗透水回收为目的的新型盐水沉淀工艺

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摘要

This research developed a three-step demineralization process for removing scale-forming compounds from brine solutions produced during nanofiltration (NF) of potable water. The process is designed to remove compounds that would produce scale and membrane fouling during further treatment via NF or reverse osmosis (RO). Jar tests were performed to determine the most suitable dosages and mixing times for each reagent. The first step in the demineralization process employs ferric chloride for removing phosphonate scale inhibitors via co-precipitation with ferric hydroxide. The second step of the process increases the solution pH value to promote carbonate mineral precipitation. The third step involves barium sulfate precipitation promoted by barite seed crystals. Saturation indices for precipitation of mineral solids were simulated using the PHREEQC thermodynamic modeling program. Water recovery from the treated brines was modeled using the ROSA package for simulating permeate and concentrate compositions for NF processes. The three-step demineralization process allowed the recovery rate for the brine solution to be as high as the initial feed water, and achieved a total water recovery of > 97%.
机译:这项研究开发了一种三步脱盐工艺,用于从饮用水的纳滤(NF)过程中产生的盐水溶液中去除水垢形成化合物。该工艺旨在去除通过NF或反渗透(RO)进行进一步处理时会产生水垢和膜污染的化合物。进行广口瓶试验以确定每种试剂的最合适剂量和混合时间。脱盐过程的第一步是使用氯化铁,通过与氢氧化铁共沉淀来去除膦酸盐阻垢剂。该方法的第二步增加溶液的pH值,以促进碳酸盐矿物的沉淀。第三步涉及由重晶石种晶体促进的硫酸钡沉淀。使用PHREEQC热力学建模程序模拟了矿物固体沉淀的饱和指数。使用ROSA软件包对从处理过的盐水中回收的水进行建模,以模拟NF工艺的渗透物和浓缩物成分。三步脱盐过程使盐水溶液的回收率与初始给水一样高,并且总水回收率> 97%。

著录项

  • 作者

    Azadi Aghdam Mojtaba;

  • 作者单位
  • 年度 2016
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  • 原文格式 PDF
  • 正文语种 en_US
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