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In situ carbonate leaching and recovery of uranium from ore deposits

机译:原位碳酸盐浸出和从矿床中回收铀

摘要

Uranium ore deposits which contain certain proportions of other metals and elemental components, such as are present in redox roll front ore deposits, are selectively leached in situ by passing therethrough relatively dilute aqueous leach solutions comprising essentially from about 0.5 to 5 grams per liter of ammonium bicarbonate and from about 0.1 to 3 grams per liter of peroxide, preferably introduced as aqueous H.sub. 2 O.sub.2, and sufficient ammonia to bring the solution to a pH of from about 7.4 to 9, and preferably from 7. 5 to 8. 5, thereafter withdrawing from the ore deposit the aqueous leach solution enriched in uranium which it preferentially extracts along with a generally lower proportion of other metals and elements as compared to their respective ratios in the ore deposit, and contacting the enriched leach solution with a strong base anion exchange material to strip the uranium from the leach solution. The uranium is eluted by treating the base anion exchange material with an aqueous eluant, and finally the uranium is recovered from the uraniferous eluate by first acidifying it and then treating with ammonia to produce a precipitate of relatively pure ammonium diuranate. The stripped leach solution is separated from the base anion exchange material and the stripped leach solution is recirculated through the ore deposit after adjusting it with more ammonium bicarbonate, peroxide and ammonia. After the uranium in the ore deposit is removed to the extent economically practicable, the leach solution is replaced with an aqueous reducing solution which is passed into the ore deposit in order to precipitate and render insoluble any uranium and elements such as vanadium, molybdenum and selenium. The process produces above ground a very low volume of impurities and waste solutions requiring disposal, and causes no significant or material contamination or deterioration of the underground deposits or any aquifer associated therewith.
机译:含有一定比例的其他金属和元素成分的铀矿床,例如氧化还原辊前矿床中存在的铀矿床,是通过使相对稀的浸出水溶液通过其中而进行浸提的,该水溶液基本上包含每升铵约0.5至5克。碳酸氢盐和每升过氧化物约0.1至3克,优选以H.sub.H.水溶液形式引入。 2 O 2和足够的氨使溶液的pH值从7.4到9,最好是从7。5到8。5,然后从矿石中抽出富含铀的浸出水溶液,与矿石中的金属和元素的比例相比,通常优先提取其他金属和元素的比例通常较低的提取物,并使富集的浸提液与强碱阴离子交换材料接触,以从浸提液中提取铀。通过用水性洗脱液处理碱性阴离子交换材料来洗脱铀,最后通过先酸化铀,然后用氨处理以产生相对纯的二铀酸铵沉淀,从铀洗出液中回收铀。将汽提的浸提溶液与基础阴离子交换材料分离,并在用更多的碳酸氢铵,过氧化物和氨进行调节后,将汽提的浸提溶液通过矿石床进行再循环。在将矿石矿床中的铀去除到经济可行的程度后,将浸提液替换为还原性水溶液,然后将其送入矿床中,以使铀和钒,钼和硒等元素沉淀并使其不溶。该方法在地面上产生需要处置的非常少量的杂质和废物溶液,并且不会引起显着或实质性污染或地下沉积物或与其相关的任何含水层的恶化。

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