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Technology of Producing of Sodium Hypochlorite from the Concentrate of Reverse Osmosis Systems

机译:利用反渗透浓缩液生产次氯酸钠的技术

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One of the modern methods of water demineralization and softening for domestic and drinking purposes as well as for its preparation in industrial production is a reverse osmosis. This demineralization method is peculiar for its concentrates that are formed due to reverse osmosis membranes and nanofiltration technologies, the utilization of which continues to be an unresolved problem. The article deals with the solution of such problem to utilize those concentrates, which are obtained using reverse osmosis and nanofiltration units. In this regard, it seems promising to reduce the volume of technological concentrate at the first stage by its repeated concentration according to nanofiltration - reverse osmosis scheme. After that, the nanofiltration concentrate containing predominantly divalent Ca~(2+), Mg~(2+) and SO_4~(2-) ions is subjected to reagent treatment in the following sequence: first stage with barium compounds and second stage with carbonate and sodium hydroxide. Such sequence allows separating from the solution at the first stage practically insoluble BaSO_4 with its precipitation in the 1st stage vortex reactor and, further precipitation of slightly soluble in alkaline medium CaCO_3 and Mg(OH)_2 in the Ⅱ stage reactor. These insoluble BaSO_4, CaCO_3 and Mg(OH)_2 salts thrown off the mass balance are finally dehydrated using a filter press and subjected to subsequent sale as a market product or raw material. The obtained solution of sodium chloride is concentrated by 3-stage reverse osmosis resulting in a 0.8-1.0% aqueous solution (8-10 g/l) of sodium chloride solution, a high-grade raw material for the production of electrolytic sodium hypochlorite with 4-6 g/l concentration by chlorine equivalent.
机译:反渗透是用于家庭和饮用水目的以及用于工业生产的水脱矿质和软化的现代方法之一。这种脱盐方法因其浓缩物而特有,该浓缩物是由反渗透膜和纳滤技术形成的,其利用仍然是一个尚未解决的问题。本文探讨了利用这些浓缩物的解决方案,这些浓缩物是使用反渗透和纳滤单元获得的。在这方面,似乎有希望通过根据纳滤-反渗透方案的反复浓缩,在第一阶段减少技术浓缩液的体积。之后,对主要包含二价Ca〜(2 +),Mg〜(2+)和SO_4〜(2-)离子的纳滤浓缩物按以下顺序进行试剂处理:第一阶段使用钡化合物,第二阶段使用碳酸盐和氢氧化钠。这样的顺序允许从第一阶段的溶液中分离出实际上不溶的BaSO 4,在第一阶段的涡旋反应器中将其沉淀,并且在第二阶段的反应器中进一步将稍溶于碱性介质CaCO 3和Mg(OH)_2的沉淀。最终从压滤机中除去的这些不溶性BaSO_4,CaCO_3和Mg(OH)_2盐最终用压滤机脱水,然后作为市售产品或原料进行销售。通过三步反渗透浓缩所得氯化钠溶液,得到0.8-1.0%的氯化钠水溶液(8-10 g / l),这是用于生产电解次氯酸钠的高级原料。按氯当量计浓度为4-6 g / l。

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