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Recovery of Co, Ni, Mo, and V from unroasted spent hydrorefining catalysts by selective chlorination

Journal Article · · Metallurgical Transactions, B (Process Metallurgy); (United States)
DOI:https://doi.org/10.1007/BF02648975· OSTI ID:6534975
;  [1]
  1. Inst. National Polytechnique de Lorraine, Vandoeuvre (France)
Spent hydrorefining catalysts may contain 4 to 6% of CoO and/or NiO, 8 to 16% of MoO[sub 3], and up to 10% of V[sub 2]O[sub 5], generally supported by alumina. They also contain up to 25% of carbon, hydrocarbons, and sulfur. Selective chlorination of raw, unroasted samples with Cl[sub 2] + air, Cl[sub 2] + N[sub 2], and Cl[sub 2] + CO + N[sub 2] gas mixtures have been investigated for the recovery of valuable elements. The fastest chlorination kinetics are obtained using the Cl[sub 2] + CO + N[sub 2] gas mixture, followed by Cl[sub 2] + N[sub 2]. The best selective chlorination of spent hydrorefining catalysts is obtained using a Cl[sub 2] + air gas mixture. At temperatures lower than 600 C, it is possible to recover more than 90% of the Ni and Co, about 99% of the Mo, and up to 75% of the V compounds. Cobalt and Nickel chlorides are extracted from the chlorination residues by their dissolution with water. Molybdenum and vanadium chlorides and/or oxychlorides are recovered by selective condensation from the vapor phase. The chlorination of the catalyst support, Al[sub 2]O[sub 3], can be limited to less than about 6%. A flow sheet is proposed.
OSTI ID:
6534975
Journal Information:
Metallurgical Transactions, B (Process Metallurgy); (United States), Journal Name: Metallurgical Transactions, B (Process Metallurgy); (United States) Vol. 26:1; ISSN MTTBCR; ISSN 0360-2141
Country of Publication:
United States
Language:
English