首页> 外国专利> Molybdenum oxide prodn. from molybdenum sulphide concentrate - by oxidn. in aq. slurry, with recirculation for higher yield and recovery of metallic impurities

Molybdenum oxide prodn. from molybdenum sulphide concentrate - by oxidn. in aq. slurry, with recirculation for higher yield and recovery of metallic impurities

机译:氧化钼产品硫化钼精矿中的氧化物。在水浆液,具有再循环功能,可提高收率并回收金属杂质

摘要

Mo oxide (MoO3) (I) prodn. by oxidn. of Mo sulphide (MoS2) concentrates (II) contg. metallic impurities (III) involves converting (II) to an aq. slurry and oxidising this in an autoclave at elevated temp. and elevated O2 partial pressure filtering off (I), neutralising the first filtrate contg. H2SO4 and filtering again. The novel feature is that a high (I) yield is obtd. and (III) are recovered by the use of the following stages: (1) Recirculation of unfiltered oxidised slurry to the slurry prepn. stage until the H2SO4) concn. reaches 80-120 (100)g/l, before filtering off (I). (2) Recirculation fo the first filtrate after neutralisation to pH 0.9-1.5(0.9) with chalk, the CaSO4 formed being filtered off to give a second filtrate (IV), and continuing until (III) are sufficiently enriched in (IV). (3) Neutralisation of (IV) to pH 2.5 with alkali hydroxide and then treating to recover Fe molybdate (V) and (III). The Mo yield is 90-100%, whilst the recovery of (III) e.g. Re and Cu, has environmental and economic advantages.
机译:氧化钼(MoO3)(I)产品被氧化。硫化钼(MoS2)精矿(II)续。金属杂质(III)涉及将(II)转化为aq。浆并在高温高压釜中氧化。和升高的O2分压滤出(I),中和第一份滤液。硫酸和再次过滤。新颖的特征是高(I)产率。 (III)通过以下步骤回收:(1)将未过滤的氧化淤浆再循环到淤浆制备物中。阶段直至H2SO4)浓度。在过滤掉(I)之前达到80-120(100)g / l。 (2)在用白垩中和至pH 0.9-1.5(0.9)后,使第一滤液再循环,滤出形成的CaSO 4,得到第二滤液(IV),并持续进行直到(III)被充分富集(IV)。 (3)用碱金属氢氧化物将(IV)中和至pH 2.5,然后进行处理以回收钼酸铁(V)和(III)。 Mo的收率为90-100%,而(III)的回收率例如为3%。稀土和铜,具有环境和经济优势。

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