METALS RECOVERY FROM SPENT SUPPORTED CATALYST

    公开(公告)号:US20230257280A1

    公开(公告)日:2023-08-17

    申请号:US17744018

    申请日:2022-05-13

    CPC classification number: C01G39/02 C01G39/006 C01G31/006 C22B7/009

    Abstract: An improved method for recovering metals from spent supported catalysts, including spent supported hydroprocessing catalysts. The method and associated processes comprising the method are useful to recover spent supported catalyst metals used in the petroleum and chemical processing industries. The method generally involves a combination of a pyrometallurgical and a hydrometallurgical method and includes forming a potassium carbonate calcine from the spent supported catalyst containing Group VIIIB/Group VIB/Group VB metal compound(s) combined with potassium carbonate, and extracting and recovering soluble Group VIB metal and soluble Group VB metal compounds from the potassium carbonate calcine.

    Process for recovery of technical grade molybdenum from diluted leaching acid solutions (PLS), with highly concentrated arsenic, from metallurgical residues
    9.
    发明授权
    Process for recovery of technical grade molybdenum from diluted leaching acid solutions (PLS), with highly concentrated arsenic, from metallurgical residues 有权
    从冶金残渣中稀释的浸出酸溶液(PLS)回收工业级钼,具有高度浓缩的砷的工艺

    公开(公告)号:US09279168B2

    公开(公告)日:2016-03-08

    申请号:US14240567

    申请日:2012-08-24

    Abstract: A method for recovering technical-grade molybdenum from diluted acid leaching solutions (PLS) that have a high arsenic concentration is disclosed. The method includes: (a) contacting a pre-filtered PLS with an anionic ion-exchange resin; (b) washing the loaded resin with water; (c) extracting molybdenum from the resin with an alkaline ammonium regenerant solution to form ammonium molybdenum in solution; (d) washing the unloaded resin with water; (e) adding iron and/or magnesium salts to the recovered ammonia solution to obtain a precipitate which is transferred to the arsenic abatement step and a solution containing ammonium molybdate; (f) adding sulphuric acid to the arsenic-free ammonia solution to precipitate ammonium molybdate; (g) separating the precipitate by filtering the molybdate and re-circulating the solution obtained with the initial PLS; (h) calcining the separated precipitate to obtain ammonia and molybdenum trioxide; and (i) recovering the released ammonia for subsequent use as a recirculated regenerant solution.

    Abstract translation: 公开了一种从具有高砷浓度的稀酸浸取溶液(PLS)中回收工业级钼的方法。 该方法包括:(a)使预过滤的PLS与阴离子离子交换树脂接触; (b)用水洗涤装载的树脂; (c)用碱性铵再生剂溶液从树脂中提取钼,以在溶液中形成钼; (d)用水清洗未加载的树脂; (e)向回收的氨溶液中加入铁和/或镁盐,以获得转移到减砷步骤中的沉淀物和含有钼酸铵的溶液; (f)向无砷氨溶液中加入硫酸使钼酸铵沉淀; (g)通过过滤钼酸盐并重新循环由初始PLS获得的溶液来分离沉淀物; (h)煅烧分离的沉淀物,得到氨和三氧化钼; 和(i)回收释放的氨以供随后使用,作为再循环再生剂溶液。

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