首页> 外国专利> METHOD OF PRODUCING DESALINATED AND DEMINERALISED WATER FOR NUCLEAR POWER PLANTS FROM SALINE WATER

METHOD OF PRODUCING DESALINATED AND DEMINERALISED WATER FOR NUCLEAR POWER PLANTS FROM SALINE WATER

机译:用盐水生产核电厂淡化除盐水的方法。

摘要

FIELD: energy.;SUBSTANCE: invention relates to production of desalinated and demineralised water for nuclear power plants. Water supply source used is waste saline water for cooling nuclear power plants, what was subjected to heating and air cooling - deaeration. Method comprises pretreatment thereof from organic substances and active chlorine on packed carbon filter 3, from suspended matter on microfilter 4 and alkali-earth elements on softening cationie filter 5, filled with cationite in Na+-form. Further desalination of water is carried out on two successive reverse-osmosis filters 7 and 10 and post-treatment on cationite 11 and 12 anionite desalinating filters with cationite and anionite in H+- and OH- forms, respectively. Filtrate of first reverse osmosis filter 7 via intermediate tank 8 is directed to input of second reverse osmosis filter 10, and part of concentrate of first reverse osmosis filter is returned to initial water tank 1, remaining volume is directed for discharge. Filtrate of second reverse osmosis filter is fed for post-treatment on cationite filter 11, and all concentrate is returned to initial water tank. Regeneration of softening cationite filter without radioactive or chemically toxic contaminants is carried out with table salt solution, and in presence said contaminants, spent cationite is directed without regeneration for conditioning and burial. Furthermore, load of softening cationite filter can be spent cationite of desalting cationite filter saturated with Na cations.;EFFECT: technical result is considerably longer service life of desalinating reverse-osmosis filters and ion-exchange filter.;1 cl, 1 dwg, 2 ex
机译:技术领域本发明涉及用于核电站的脱盐和去离子水的生产。所使用的供水源是用于冷却核电站,经过加热和空气冷却的除盐水废水。该方法包括从填充碳过滤器3上的有机物和活性氯,从微过滤器4上的悬浮物和软化阳离子过滤器5上的碱土元素进行预处理,其中Na +(Sup)+ 形式的阳离子盐填充其中。在两个连续的反渗透过滤器7和10上对水进行进一步的脱盐处理,并在H + -和OH - 表格。经由中间槽8将第一反渗透过滤器7的滤液引导至第二反渗透过滤器10的输入,并将第一反渗透过滤器的浓缩物的一部分返回至初始水槽1,将剩余的体积引向排出。将第二反渗透过滤器的滤液送入阳离子滤池11进行后处理,所有浓缩液返回初始水箱。用食盐溶液对没有放射性或化学毒性污染物的软化阳离子过滤器进行再生,并且在存在所述污染物的情况下,将废阳离子直接导向而无需再生以进行调节和埋葬。此外,软化的阳离子过滤器的负荷可以用饱和了Na阳离子的脱盐阳离子过滤器中的阳离子来代替。效果:技术成果是使反渗透过滤器和离子交换过滤器脱盐的使用寿命大大延长; 1 cl,1 dwg,2前

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