Platinum recovery from a spent industrial dehydrogenation catalyst using cyanide leaching followed by ion exchange

被引:64
作者
Shams, K
Beiggy, MR
Shirazi, AG
机构
[1] Isfahan Univ Technol, Dept Chem Engn, Esfahan 84154, Iran
[2] Iran Chem Ind Invest Co ICIIC, Dept Res & Dev, Esfahan, Iran
关键词
anionic resin; cyanide; ion exchange; leaching; platinum; spent catalysts; cyanoplatinate complex;
D O I
10.1016/j.apcata.2003.09.003
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Recovery of platinum from a selective linear paraffin dehydrogenation spent catalyst is reported using cyanide leaching method followed by adsorption of the cyanide platinum complex onto an anionic resin. The resin on which the platinum complex is adsorbed is dried and burned in an oxidizing, atmosphere at 800-850degreesC. The recovered metallic powder is mainly platinum. Results show that presence of coke does not have adverse effect on platinum recovery in cyanide leaching process, and in practice there is no need for decoking of spent catalysts in this method. Various parameters of interest are studied and the optimum conditions for highest platinum recovery are reported. (C) 2003 Elsevier B.V. All rights reserved.
引用
收藏
页码:227 / 234
页数:8
相关论文
共 24 条
  • [1] Allen R. J., 1992, U.S. Patent, Patent No. 5102632
  • [2] Ammen CW, 1997, RECOVERY REFINING PR
  • [3] ANJELIDIS TN, 1996, APPL CATAL A-GEN, V142, P387
  • [4] [Anonymous], [No title captured], Patent No. [5,431,892, 5431892]
  • [5] Atkinson G.B., 1992, Patent No. [5160711A, 5160711]
  • [6] BENEFIELD LD, 1982, PROCESS CHEM WATER W, P414
  • [7] Cichy P., 1982, U.S. Patent, Patent No. [4,337,085, 4337085]
  • [8] De Boer G., 1994, U.S. Patent, Patent No. 5302183
  • [9] DICKERSON RE, 1984, CHEM PRINCIPLE, P321
  • [10] FOGEL W, 1998, Patent No. 5783062