Sulfuric acid baking and leaching of spent Co-Mo/Al 2O 3 catalyst

Abstract

Dissolution of metals from a pre-oxidized refinery plant spent Co-Mo/Al 2O 3 catalyst have been tried through low temperature (200–450 °C) sulfuric acid baking followed by mild leaching process. Direct sulfuric acid leaching of the same sample, resulted poor Al and Mo recoveries, whereas leaching after sulfuric acid baking significantly improved the recoveries of above two metals. The pre-oxidized spent catalyst, obtained from a Korean refinery plant found to contain 40% Al, 9.92% Mo, 2.28% Co, 2.5% C and trace amount of other elements such as Fe, Ni, S and P. XRD results indicated the host matrix to be poorly crystalline γ- Al 2O 3. The effect of various baking parameters such as catalyst-to-acid ratio, baking temperature and baking time on percentage dissolutions of metals has been studied. It was observed that, metals dissolution increases with increase in the baking temperature up to 300 °C, then decreases with further increase in the baking temperature. Under optimum baking condition more than 90% Co and Mo, and 93% Al could be dissolved from the spent catalyst with the following leaching condition: H 2SO 4 = 2% (v/v), temperature = 95 °C, time = 60 min and Pulp density = 5%.