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process for recovering valuable amount of refractory metals

机译:回收宝贵数量的难熔金属的方法

摘要

1359245 Recovering metal values CONTINENTAL ORE CORP 23 May 1972 [18 June 1971] 24318/72 Heading C1A V, Mo, W, Ti and Nb metal values are recovered from their concentrates by forming an aq. soln. of the metal, 80% of which is in the highest oxidation state, adding to the soln. FeSO 4 or FeCl 3 in an amount to provide an Fe/metal mass ratio of 0À1-1À0, precipitating a metal/Fe/ammine complex at a pH of 2À5-4À0 in the presence of NH 4 SP+/SP ion in an amount to provide a NH 4 SP+/SP/metal mass ratio of 0À05-1À6, and then recovering the complex ppt. from the soln. Finely divided carbon may be dispersed in the soln. in an amount to provide a C/metal mass ratio of 0À6-0À8 to produce a carbon-containing ppt. The NH 4 SP+/SP ion may be added to the soln. as (NH 4 ) 2 SO 4 , NH 4 Cl or aq. NH 3 . The resultant aq. soln. obtained after recovery of the ppt. may be further treated by the addition of more ferric salt in an amount to provide a Fe/metal mass ratio of 0À5-3À0 thereby to ppt. additional complex which may be recovered or dissolved in an aq. soln. of H 2 SO 4 or HCl, and then the dissolved complex recycled to the initial pptn. step. The initial aq. soln. of metal values may be obtained from their concentrates by fusing the concentrate with Na 2 CO 3 , leaching the fused mixture with water to produce an alkaline liquor, leaching the solid residue from the aq. leach with H 2 SO 4 to produce an acidic liquor and then combining the two leach solns. The acidic liquor may be used to dissolve the additional complex ppt. The dried ppt. may be reduced at elevated temp. to produce a metallic additive suitable for use in steel-making.
机译:1359245恢复金属价值CONTINENTAL ORE CORP 1972年5月23日[1971年6月18日] 24318/72品目C1A V,Mo,W,Ti和Nb通过形成水溶液来从其精矿中恢复。 soln。的金属中,有80%处于最高氧化态,并添加到了金属溶液中。 FeSO 4或FeCl 3的含量要使铁/金属的质量比为0-1-1-1-0,在NH 4 + 的存在下,在pH值为2-5-4-0时会沉淀出金属/铁/氨合物。离子的量可以使NH 4 + /金属质量比为0‑05-1‑6,然后回收复杂的ppt。从Soln。细碎的碳可能会分散在溶液中。碳/金属质量比为0‑6-0‑8以产生含碳的ppt。可以将NH 4 + 离子添加到溶液中。以(NH 4)2 SO 4,NH 4 Cl或aq。 NH 3。所得的水溶液。 soln。在ppt恢复后获得。可以通过添加更多的铁盐来进一步处理铁盐,其量应使铁/金属的质量比为0-5至3-0。可能被回收或溶解在水溶液中的其他配合物。 soln。取H 2 SO 4或HCl,然后将溶解的络合物再循环至初始pptn。步。初始水soln。可以通过将精矿与Na 2 CO 3熔融,将熔融的混合物用水浸出以产生碱性液,从水溶液中浸出固体残渣来从其精矿中获得最大的金属价值。用H 2 SO 4浸提产生酸性液体,然后将两种浸提液合并。酸性液体可用于溶解另外的复合物ppt。干的ppt。在高温下可能会降低。生产适用于炼钢的金属添加剂。

著录项

  • 公开/公告号IT958238B

    专利类型

  • 公开/公告日1973-10-20

    原文格式PDF

  • 申请/专利权人 CONTINENTAL ORE CORP;

    申请/专利号IT19720050731

  • 发明设计人

    申请日1972-06-07

  • 分类号C22B;

  • 国家 IT

  • 入库时间 2022-08-23 07:32:05

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