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process for the concentration of uranium in the slag, phosphorus furnace, for the subsequent extraction of uranium

机译:炉渣中浓缩铀的工艺,磷炉,用于随后的铀提取

摘要

Uranium values are recovered from slags derived from the reduction of phosphates in the presence of silica, by subjecting to acid attack so that the calcareous constituents are dissolved, leaving the uranium in the solid residue from which it can be extracted. The slag is ground so that all of it can pass through a Tyler 150 mesh screen and is diluted with an approximately equal weight of water. Acid is added to the agitated pulp, local concentrations of acid being avoided by successive small additions or slow continuous addition. The acid may be hydrochloric, nitric, perchloric or phosphoric. The uranium content in the solid residue may be recovered by conventional attack with sulphuric acid or sodium carbonate, or it may be re-used as part the charge to the phosphorus reduction furnace so as to enrich the silica slag with respect to uranium.ALSO:A process for the recovery of uranium wherein slags derived from the reduction of phosphates in the presence of silica are subjected to a mode of acid attack such that the calcareous constituents are dissolved while leaving the uranium in a solid residue from which the uranium can be extracted. The slag is ground so that all of it can pass through a Tyler 150 mesh screen and is diluted with an approximately equal weight of water. Acid is added to the agitated pulp, local concentrations of acid being avoided by successive small additions or slow continuous addition. The acid may be hydrochloric, nitric, perchloric or phosphoric, the latter being included at the rate of 5-15 litres per ton of slag if another acid is used when a low content of P2O5 in the slag could cause serious risk of the calcium salt produced being discoloured by ferric ions. The strength of the acid used is 5-6 N and the attack lasts at least one hour, the temperature being maintained at 70-80 DEG C., and the final pH of the pulp being 2-3. The precipitate from the reaction is washed in counter-current using 6-8 cubic meters of water per ton of slag. The uranium content in the solid residue may be recovered by conventional attack with sulphuric acid or sodium carbonate, or it may be re-used as part the charge to the phosphorus reduction furnace so as to enrich the silica slag with respect to uranium. p
机译:通过对硅酸进行酸侵蚀,从二氧化硅还原过程中从磷酸盐还原产生的炉渣中回收铀值,从而使钙质成分溶解,从而使铀残留在固体残留物中,可以从中提取铀。将炉渣磨碎,使所有炉渣都能通过Tyler 150筛网,并用大约等量的水稀释。将酸添加到搅拌的果肉中,通过连续少量添加或缓慢连续添加来避免酸的局部浓度。酸可以是盐酸,硝酸,高氯酸或磷酸。固体残渣中的铀含量可以通过常规的硫酸或碳酸钠攻击来回收,也可以作为一部分进料再用于磷还原炉中,以富集相对于铀的硅渣。一种回收铀的方法,其中使在二氧化硅存在下源自磷酸盐还原的炉渣经受酸攻击模式,使钙质成分溶解,同时将铀留在可从中提取铀的固体残渣中。将炉渣磨碎,使所有炉渣都能通过Tyler 150筛网,并用大约等量的水稀释。将酸添加到搅拌的果肉中,通过连续少量添加或缓慢连续添加来避免酸的局部浓度。酸可以是盐酸,硝酸,高氯酸或磷酸,如果在渣中低含量的P2O5可能导致严重的钙盐风险时使用另一种酸,则以每吨矿渣5-15升的速率包含后者。产生的被铁离子褪色。所用酸的强度为5-6N,并且侵蚀持续至少一小时,温度保持在70-80℃,并且纸浆的最终pH为2-3。来自反应的沉淀物使用每吨炉渣6-8立方米的水逆流洗涤。固体残余物中的铀含量可以通过常规的硫酸或碳酸钠的攻击来回收,或者可以作为进料到磷还原炉中的一部分再利用,以使硅渣相对于铀富集。 p

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