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    • 2. 发明授权
    • Recovery of metal values from spent hydrodesulfurization catalysts
    • 从废加氢脱硫催化剂中回收金属值
    • US4495157A
    • 1985-01-22
    • US528884
    • 1983-09-02
    • Roger F. SebenikPablo P. LaValleJohn M. LafertyWilliam A. May
    • Roger F. SebenikPablo P. LaValleJohn M. LafertyWilliam A. May
    • C01F7/02C01G31/00C01G39/00C01G51/04C01G53/04C22B3/28C22B7/00C22B34/22C22B34/34
    • C01G39/003C01F7/02C01G31/003C01G51/04C01G53/04C22B3/0012C22B3/0016C22B34/22C22B34/34C22B7/008C01P2006/80Y02P10/234
    • A process is provided for recovering metal values from spent hydrodesulfurization catalyst, the process comprising forming in a pressure reactor an aqueous slurry of finely divided spent catalyst and sodium carbonate, the spent catalyst containing by weight about 2 to 10% Mo, up to about 12% V (e.g., about 2 to 10%), about 0.5 to 4% Co, up to about 10% Ni (e.g., about 0.5 to 5%), occluded oil, coke, sulfide sulfur and the balance essentially alumina. The amount of sodium carbonate employed is at least sufficient under oxidizing conditions to convert molybdenum and any vanadium present to soluble Na.sub.2 MoO.sub.4 and NaVO.sub.3 and to neutralize SO.sub.3 produced during oxidation, the amount of sodium carbonate being at least that required stoichiometrically. The slurry is heated to a temperature of about 200.degree. C. to 350.degree. C. (e.g., 275.degree. C. to 325.degree. C.) and a pressure of about 800 psig to 2500 psig (e.g., about 1500 psig to 2500 psig) for a time at least sufficient to solubilize the molybdenum and vanadium present, the amount of oxygen employed being over about 1.1 times the stoichiometric amount sufficient to oxidize the metal values and sulfur to the maximum oxidized state, and to oxidize the oil and free carbon to CO.sub.2 and H.sub.2 O. The solubilized Mo and V are thereafter separated from each other.
    • 提供了用于从废加氢脱硫催化剂中回收金属值的方法,该方法包括在压力反应器中形成细分散的废催化剂和碳酸钠的含水浆料,废催化剂含有约2至10%Mo至多约12 %V(例如约2至10%),约0.5至4%Co,至多约10%Ni(例如约0.5至5%),封闭油,焦炭,硫化物硫和余量基本为氧化铝。 使用的碳酸钠的量在氧化条件下至少足以将存在的钼和任何钒转化成可溶性Na 2 MoO 4和NaVO 3,并中和氧化期间产生的SO 3,碳酸钠的量至少为化学计量所需的量。 将浆料加热至约200℃至350℃(例如275℃至325℃)和约800psig至2500psig(例如约1500psig至2500psig)的压力 )至少足以溶解存在的钼和钒,使用的氧气的量超过足以将金属值和硫氧化成最大氧化态的化学计量量的约1.1倍,并且使油和游离碳氧化 到CO2和H2O。 然后将溶解的Mo和V彼此分离。
    • 3. 发明授权
    • Production of molybdenum oxide from ammonium molybdate solutions
    • 钼酸铵溶液生产氧化钼
    • US4273745A
    • 1981-06-16
    • US81412
    • 1979-10-03
    • John M. LafertyDennis L. HoweRoger F. Sebenik
    • John M. LafertyDennis L. HoweRoger F. Sebenik
    • C01G39/00C01G39/02
    • C01G39/003C01G39/02C01P2006/80
    • Molybdenum is recovered from an ammonium molybdate solution containing phosphate anions by digesting in an ammonium molybdate solution at least one water-soluble compound of at least one metal selected from the group consisting of aluminum, calcium, iron and magnesium in small but effective amounts to precipitate at least about 50% of the phosphate anions for a time sufficient to precipitate the phosphate anion, separating the phosphate precipitate from the ammonium molybdate solution, then acidifying the ammonium molybdate solution with at least one mineral acid selected from the group consisting of sulfuric acid and nitric acid to lower the pH value of the solution to between about 2.5 and about 4.5 to precipitate ammonium polymolybdate, and calcining the ammonium polymolybdate at a temperature below about 750.degree. C. to produce a molybdenum trioxide product.
    • 通过在钼酸铵溶液中消化至少一种选自铝,钙,铁和镁的至少一种金属的水溶性化合物,以少量但有效的量沉淀,从含有磷酸根阴离子的钼酸铵溶液中回收钼 至少约50%的磷酸盐阴离子足以沉淀磷酸盐阴离子,将钼酸铵溶液中的磷酸盐沉淀物分离出来,然后用至少一种无机酸酸化钼酸铵溶液,所述无机酸选自硫酸和 硝酸以将溶液的pH值降低至约2.5至约4.5之间以沉淀多钼酸铵,并在低于约750℃的温度下煅烧多钼酸铵以产生三氧化钼产物。