Recovery of vanadium and molybdenum from heavy oil desulphurization waste catalyst |
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Authors: | RK Biswas M Wakihara M Taniguchi |
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Affiliation: | Department of Applied Chemistry, Rajshahi University Bangladesh;Department of Chemical Engineering, Tokyo Institute of Technology, O-okayama, Meguro-ku, Tokyo Japan |
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Abstract: | Sodium chloride-water vapour roasting of calcined catalyst for 2 h at 850°C (water vapour pressure 0.253 bar, N2 atmosphere) and subsequent leaching of the roasted catalyst with water at its boiling point for 1 h dissolved 81.85% V and 81.78% Mo and minor amounts of other constituents. The separation of V from the leach solution has been carried out efficiently by precipitation (as NH4VO3), liquid-liquid extraction using di(2-ethylhexyl)phosphoric acid (D2EHPA) and tri-n-octylamine (TOA) and subsequent strippings and precipitations. The overall recoveries of V and Mo from the waste catalyst are 75.5 and 77%, respectively. |
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Keywords: | To whom correspondence should be addressed |
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