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Tandom reverse osmosis process for zero-liquid discharge

机译:串联反渗透工艺实现零液体排放

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摘要

Major sources of wastewater generated on land can benefit from, and often are in need of, processes for the complete recovery of water, having only solid by-products or waste for disposal. This applies to municipal and industrial wastewater and brackish water reverse osmosis (RO) plants and agricultural irrigation. High recovery of water with RO membranes is by far the most efficient method of processing waste and brackish water. Recoveries ranging from 70 to 90% are possible, limited by precipitation of insoluble salts and coagulation of colloidal particles. If emerging intermediate precipitative treatments of the limiting foulants can become widely successful, a tandom second RO step of similar recovery rates will reach an overall water recovery of 97-99%. The remaining 1-3% of the original water volume can be addressed with evaporative concentrators. Based on our initial successes, we clearly see this tandom RO process to be of universal utility. Precipitated salts from the treatment of the primary RO concentrate are mainly divalent cations (Ca, Mg, Sr, Ba) with coagulated silica and colloidal matter. Solutes that survive the secondary RO are mainly soluble monovalent cations (Na, K). The overall tandom RO process thus constitutes a way to fractionate divalent cation salts from the monovalent cation salts. Both salt fractions may find commercial use and not be entirely wasted. We currently are actively assisting municipal RO plants in California in maximizing the percent recovery in the primary ROs, and for the moment, minimizing the volumes of raw water needed and volumes of concentrate that have to be discharged. To illustrate the necessity of dealing with the unique water chemistry of each RO plant, we present the well water analyses of three municipal systems within a 25-mile radius of Riverside, CA. In each case, due to the high cost of discharging concentrate into a brine line to the sea, close to limiting primary RO recoveries have been reached. The results of autopsies and foulant analyses performed on membranes from these three plants identify the foulants that need to be precipitatively removed before treatment with secondary RO. Further work is being considered along these lines.
机译:陆地上产生的废水的主要来源可以从(通常需要)完全回收水的过程中受益,并且常常需要这些过程,而这些过程仅具有固体副产物或废物进行处置。这适用于市政和工业废水和微咸水反渗透(RO)厂和农业灌溉。迄今为止,使用反渗透膜对水进行高回收率是处理废水和微咸水的最有效方法。由于不溶性盐的沉淀和胶体颗粒的凝结,回收率可能在70%到90%之间。如果新兴的限制污垢的中间沉淀处理能够获得广泛成功,那么具有相似回收率的第二反渗透步骤将达到97-99%的总水回收率。剩余的1-3%的原始水可用蒸发浓缩器处理。根据我们的初步成功,我们清楚地看到这种切合的RO工艺具有通用性。处理初级反渗透浓缩物时沉淀出的盐主要是二价阳离子(Ca,Mg,Sr,Ba),并带有凝结的二氧化硅和胶体。在次要RO中存活的溶质主要是可溶性单价阳离子(Na,K)。因此,总的正切RO过程构成了从单价阳离子盐中分离二价阳离子盐的方法。两种盐馏分都可以找到商业用途,而不是完全浪费。我们目前正在积极协助加利福尼亚州的市政RO工厂最大限度地提高主要RO中的回收率,目前,将所需原水量和必须排放的精矿量降至最低。为了说明处理每个反渗透工厂独特的水化学性质的必要性,我们介绍了加利福尼亚州里弗赛德方圆25英里范围内的三个市政系统的井水分析。在每种情况下,由于将精矿排入盐水线排放到海中的成本很高,因此已经接近接近限制的主要反渗透率。在这三座工厂的膜上进行的尸检和污垢分析结果表明,在进行二次RO处理之前,必须先去除这些污垢。正在沿着这些思路考虑进一步的工作。

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