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Schemes for salt recovery from seawater and RO brines using chemical precipitation

机译:使用化学沉淀法从海水和反渗透盐水中回收盐的方案

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Disposal of brines from seawater desalination plants affects marine ecology and significant financial burdens. Recovery of salts from brines improves both sides of the problem and avails opportunities for new state of the art desalination/salt production complex. Three important separation processes could be adopted to formulate the corner stones for state-of-the-art salt recovery production line, namely chemical treatment, nanofiltration (NF), and ion exchange. This paper explores the performance of selected precipitants on saline solutions presenting synthetic seawater, natural seawater, and two reverse osmosis (RO) brines obtained from desalination plants located on Mediterranean (B1) and Red Sea (B2) shores. Sodium carbonate enabled 95.5, 89, and 95% recovery of calcium (Ca) seawater, Mediterranean, and Red Sea RO brines, respectively. While, values of magnesium (Mg) recovery from chemically treated schemes lie between 85.6 and 91.3%. Also, phosphate precipitation enabled two-stage recovery of Ca and Mg range from 75 to 98% for Ca and 24 to 47% for Mg. Moreover, analysis of our experimental results and other reported data on chemical softening enabled identification of three integrated salt recovery schemes from seawater and RO desalination brines. The first scheme is basically applicable for new desalting plants or even as stand-alone solution for chemical recovery from seawater. The second scheme could be applied when retrofitting current desalination plants where state-of-the-art NF is introduced and the generated NF brine is subjected to two-stage chemical and ion exchange treatments. The third scheme targets currently operating plants where RO brines could be directed to chemical precipitation for maximum Ca removal and subsequently decalcified streams could be processed for Mg removal using ion exchange. Optimization of the developed schemes is currently underway to identify comparative capital outlays and other relevant financial indicators.
机译:海水淡化厂处理盐水的处理会影响海洋生态和重大的财务负担。从盐水中回收盐可改善问题的两面,并为新的现有技术脱盐/盐生产综合设施提供了机会。可以采用三个重要的分离工艺来配制最先进的盐回收生产线的基石,即化学处理,纳滤(NF)和离子交换。本文探讨了沉淀剂在含合成海水,天然海水和两种反渗透(RO)盐水的盐溶液中的性能,这些盐溶液来自位于地中海(B1)和红海(B2)海岸的海水淡化厂。碳酸钠可分别回收95.5%,89%和95%的钙(Ca)海水,地中海和红海RO盐水。而从化学处理方案中回收的镁(Mg)值介于85.6%和91.3%之间。同样,磷酸盐沉淀使钙和镁的两阶段回收率从钙的75%到98%,镁的24%到47%不等。此外,对我们的实验结果和其他有关化学软化的数据进行分析后,可以识别出三种从海水和反渗透淡化盐水中回收盐的综合方案。第一种方案基本上适用于新的脱盐工厂,甚至可作为从海水中回收化学药品的独立解决方案。当改造现有的脱盐工厂时,可以采用第二种方案,在脱盐工厂中引进了最先进的NF装置,并将生成的NF盐水进行两阶段的化学和离子交换处理。第三个方案针对当前正在运行的工厂,在这些工厂中,可以将RO盐水引导至化学沉淀以最大程度地去除Ca,随后可以通过离子交换处理脱钙的水流以去除Mg。目前正在对已开发计划进行优化,以确定可比较的资本支出和其他相关财务指标。

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