Separation of Mo from Chloride Leach Liquors of Petroleum Refining Catalysts by Ion Exchange

被引:4
作者
Thi Hong Nguyen [1 ]
Sohn, Seong Ho [2 ]
Lee, Man Seung [1 ]
机构
[1] Mokpo Natl Univ, Dept Adv Mat Sci & Engn, Chungnam 534729, South Korea
[2] Korea Inst Ind Technol, Incheon Technol Serv Ctr, Inchon 406840, South Korea
关键词
molybdenum; cobalt; aluminum; separation; ion exchange; AG1-x8; Diphonix; SULFURIC-ACID-SOLUTION; RECOVERY; MOLYBDENUM; VANADIUM; EXTRACTION; CO;
D O I
10.2320/matertrans.M2013141
中图分类号
T [工业技术];
学科分类号
08 ;
摘要
Separation of molybdenum from the synthetic chloride leach liquors of spent hydrodesulphurization catalysts was studied by employing cationic (Diphonix) and anionic resins (AG1-x8). The composition of the solution was Mo 394 ppm, Co 119 ppm and Al 1782 ppm. In the HCl concentration range from 1 to 6 kmol/m(3), the loading of Co and Al was negligible. As the concentration of HCl increased, the loading percentage of Mo by AG1-x8 increased, while that by Diphonix decreased. The Mo in the loaded AG1-x8 was successfully eluted by using NaOH solution. In terms of the possibility of producing Mo compound from the eluant, AG1-x8 was found to be better than Diphonix. The loading capacity of AG1-x8 for molybdenum was determined. Column experiments verified that it was possible to separate Mo from Co and Al by ion exchange with AG1-x8.
引用
收藏
页码:1750 / 1754
页数:5
相关论文
共 20 条
  • [1] Solvent Extraction Separation of Mo and Co from Chloride Solution Containing Al
    Banda, Raju
    Sohn, Seong Ho
    Lee, Man Seung
    [J]. MATERIALS TRANSACTIONS, 2013, 54 (01) : 61 - 65
  • [2] Recovery of valuable metals and regeneration of acid from the leaching solution of spent HDS catalysts by solvent extraction
    Banda, Raju
    Nguyen, Thi Hong
    Sohn, Seong Ho
    Lee, Man Seung
    [J]. HYDROMETALLURGY, 2013, 133 : 161 - 167
  • [3] Process development for the separation and recovery of Mo and Co from chloride leach liquors of petroleum refining catalyst by solvent extraction
    Banda, Raju
    Sohn, Seong Ho
    Lee, Man Seung
    [J]. JOURNAL OF HAZARDOUS MATERIALS, 2012, 213 : 1 - 6
  • [4] Direct leaching of molybdenum and cobalt from spent hydrodesulphurization catalyst with sulphuric acid
    Barik, S. P.
    Park, Kyung-Ho
    Parhi, P. K.
    Park, J. T.
    [J]. HYDROMETALLURGY, 2012, 111 : 46 - 51
  • [5] Ionic Equilibria and Ion Exchange of Molybdenum(VI) from Strong Acid Solution
    Lee, Manseung
    Sohn, Seongho
    Lee, Myungho
    [J]. BULLETIN OF THE KOREAN CHEMICAL SOCIETY, 2011, 32 (10) : 3687 - 3691
  • [6] Co-extraction and selective stripping of vanadium (IV) and molybdenum (VI) from sulphuric acid solution using 2-ethylhexyl phosphonic acid mono-2-ethylhexyl ester
    Li, Xingbin
    Wei, Chang
    Wu, Jun
    Li, Minting
    Deng, Zhigan
    Li, Cunxiong
    Xu, Hongsheng
    [J]. SEPARATION AND PURIFICATION TECHNOLOGY, 2012, 86 : 64 - 69
  • [7] Mihashi T., 1982, Japanese Pat, Patent No. 57022119
  • [8] Bioleaching of vanadium rich spent refinery catalysts using sulfur oxidizing lithotrophs
    Mishra, D.
    Kim, D. J.
    Ralph, D. E.
    Ahm, J. G.
    Rhee, Y. H.
    [J]. HYDROMETALLURGY, 2007, 88 (1-4) : 202 - 209
  • [9] Recovery of metal values from spent petroleum catalyst using leaching-solvent extraction technique
    Mishra, Debaraj
    Chaudhury, G. Roy
    Kim, Dong J.
    Ahn, Jong G.
    [J]. HYDROMETALLURGY, 2010, 101 (1-2) : 35 - 40
  • [10] Nguyen T. H., 2013, HYDROMETALL IN PRESS