首页> 外国专利> METHOD FOR RECOVERING TECHNICAL-GRADE MOLYBDENUM FROM DILUTED ACID LEACHING SOLUTIONS (PLS) THAT HAVE A HIGH ARSENIC CONCENTRATION AND ORIGINATE FROM METALLURGICAL WASTE.

METHOD FOR RECOVERING TECHNICAL-GRADE MOLYBDENUM FROM DILUTED ACID LEACHING SOLUTIONS (PLS) THAT HAVE A HIGH ARSENIC CONCENTRATION AND ORIGINATE FROM METALLURGICAL WASTE.

机译:从具有高砷浓度且源自冶金废料的稀酸浸出液(PLS)中回收工业级钼的方法。

摘要

The invention relates to a method for recovering technical-grade molybdenum from diluted acid leaching solutions (PLS) that have a high arsenic concentration, said method comprises the following steps consisting in: (a) bringing a pre-filtered acid leaching solution (PLS), originating from the leaching of smelter dust, into contact with an anionic ion-exchange resin; (b) washing the loaded resin with water; (c) extracting the molybdenum from the ion-exchange resin with an alkaline ammonium regenerant solution at a pH value of between 8 and 12, in order to form ammonium molybdenum in solution; (d) washing the unloaded resin with water; (e) adding iron and/or magnesium salts to the recovered ammoniacal solution, in order to obtain a precipitate which is transferred to the arsenic abatement step and a solution containing ammonium molybdate in solution; (f) adding sulphuric acid to the arsenic-free ammoniacal solution in order to precipitate the moylbdenum in the form of ammonium molybdate in an acid environment at a pH value of between 1.5 and 4; (g) separating the precipitate formed by filtering the molybdate and re-circulating the solution obtained with the initial PLS solution; (h) calcining the separated precipitate in order to obtain ammonia and molybdenum trioxide; and (i) recovering the released ammonia for its subsequent use in the method as a recirculated regenerant solution.
机译:本发明涉及一种从砷含量高的稀酸浸出液(PLS)中回收工业级钼的方法,所述方法包括以下步骤:(a)将预过滤的酸浸出液(PLS)引入源自冶炼厂粉尘的浸出,与阴离子交换树脂接触; (b)用水洗涤负载的树脂; (c)用pH 8至12的碱性铵再生溶液从离子交换树脂中提取钼,以便在溶液中形成钼铵; (d)用水洗涤卸载的树脂; (e)将铁和/或镁盐添加到回收的氨溶液中,以获得沉淀物,该沉淀物被转移至减砷步骤和溶液中含有钼酸铵的溶液中; (f)在无砷的氨溶液中加入硫酸,以使钼酸铵形式的钼在pH值为1.5至4的酸性环境中沉淀; (g)分离通过过滤钼酸盐而形成的沉淀物,并使用初始PLS溶液获得的溶液再循环; (h)煅烧分离出的沉淀以获得氨和三氧化钼; (i)回收释放的氨,以供随后在该方法中用作再循环的再生剂溶液。

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