PROCESS FOR THE COMPREHENSIVE RECOVERY OF METAL COBALT, RUTHENIUM AND ALUMINUM FROM WASTE CATALYST CO-RU/AL2O3 IN FISCHER-TROPSCH SYNTHESIS
    6.
    发明公开
    PROCESS FOR THE COMPREHENSIVE RECOVERY OF METAL COBALT, RUTHENIUM AND ALUMINUM FROM WASTE CATALYST CO-RU/AL2O3 IN FISCHER-TROPSCH SYNTHESIS 有权
    PROCEDURE用于金属钴,钌和铝的从废催化剂CO RU / Al2O3的AT费 - 托工艺完全恢复

    公开(公告)号:EP2824200A1

    公开(公告)日:2015-01-14

    申请号:EP13758445.4

    申请日:2013-03-04

    IPC分类号: C22B7/00

    摘要: Provided is a process for the comprehensive recovery of metal cobalt, ruthenium and aluminum from a waste catalyst Co-Ru/Al 2 O 3 in a Fischer-Tropsch synthesis. First, a waste catalyst is subjected to hydrocarbon removal, and reduction treatment, to effectively separate a cobalt slag in an alkali fusion step, and then the cobalt slag is subjected to the steps of acid leaching, cobalt precipitation with oxalic acid or ammonium oxalate, reduction of cobalt oxalate, dissolution of metal cobalt with nitric acid, etc., to obtain Co(N0 3 ) 2 ·6H 2 O. A ruthenate which is dissolved by steps such as alkali fusion, and leaching with deionized water, is subjected to the steps of reduction with ethanol, dissolution with concentrated hydrochloric acid, distillation under reduced pressure, etc., to obtain a β-RuCl 3 ·xH 2 O product with a high purity. Aluminum hydroxide is prepared from a meta-aluminate solution by CO 2 carbonation, by controlling the parameters such as reaction temperature, flow rate of CO 2 , pH value at the end point of the reaction, etc., and the aluminum hydroxide is calcined to obtain aluminum oxide with a product quality achieving the quality requirements of first-class aluminum oxide in the Chinese national standard. The resulting product has a high yield, wherein cobalt is ≥ 97%, ruthenium is ≥ 95%, and aluminum is ≥ 92%.

    摘要翻译: 本发明提供用于从废催化剂共同的Ru /的Al 2 O 3在费 - 托合成金属钴,钌和铝的综合回收的方法。 首先,将废弃物催化剂进行烃脱除,和还原处理,在超过碱熔步骤有效地分离钴炉渣,然后将钴炉渣进行酸浸出,钴沉淀的步骤用草酸或草酸铵, 减少草酸盐的钴,金属钴溶解用硝酸等,以获得的Co(NO 3)2·6H 2 O的钌所有这是由溶解的步骤:如碱熔,并与去离子水沥滤,进行 在减压下等,还原用乙醇,溶解,用浓盐酸,蒸馏的步骤,以得到一个²-的RuCl 3·XH 2 O产物具有高纯度。 氢氧化铝是由偏铝溶液通过CO 2碳酸化制备,通过控制参数:如反应温度,流量的CO 2的速率,在反应中,等,且氢氧化铝的终点PH值煅烧以 获得与产品质量实现一流的氧化铝在中国国家标准的质量要求氧化铝。 所得到的产品具有高的产率,worin钴是‰¥97%,钌是‰¥95%,铝是‰¥92%。

    Value recovery from spent alumina-base catalysts
    8.
    发明公开
    Value recovery from spent alumina-base catalysts 失效
    Tonerde enthaltenden Katalysatoren的Rückgewinnungvon Wertstoffen aus gebrauchten。

    公开(公告)号:EP0241149A2

    公开(公告)日:1987-10-14

    申请号:EP87302119.0

    申请日:1987-03-12

    发明人: Hyatt, David E.

    摘要: A process for the recovery of aluminum and at least one other metal selected from the group consisting of molybdenum, nickel and cobalt from a spent hydrogenation catalyst comprising (1) adding about 1 to 3 parts H₂SO₄ to each part of spent catalyst in a reaction zone of about 20° to 200°C under sulfide gas pressure between about 1 and about 35 atmospheres, (2) separating the resultant Al₂(SO₄)₃ solution from the sulfide precipitate in the mixture, (3) oxidizing the remaining sulfide precipitate as an aqueous slurry at about 20° to 200°C in an oxygen-­containing atmosphere at a pressure between about 1 and about 35 atmospheres, (4) separating the slurry to obtain solid molybdic acid and a sulfate liquor containing said at least one metal, and (5) recovering said at least one metal from the sulfate liquor in marketable form.

    摘要翻译: 一种从废氢化催化剂中回收铝和至少一种选自钼,镍和钴的其它金属的方法,包括(1)在反应区中的每一部分废催化剂中加入约1至3份H 2 SO 4 在约1至约35个大气压之间的硫化氢气压下约20℃至200℃,(2)从混合物中的硫化物沉淀物分离得到的Al 2(SO 4)3溶液,(3)将剩余的硫化物沉淀物氧化为 在约20至200℃的含氧气氛中,在约1至约35个大气压之间的压力下,(4)分离浆料以获得固体钼酸和含有所述至少一种金属的硫酸盐液体,以及 (5)以可销售的形式从所述硫酸液体中回收所述至少一种金属。