Selective extraction of molybdenum and vanadium from spent catalysts by oxidative leaching with sodium aluminate and caustic
AssigneeAmax Inc.
InventorEdward I. Wiewiorowski
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AssigneeAmax Inc.
InventorEdward I. Wiewiorowski
Estimating the term…
Spent hydrodesulfurization catalysts containing alumina, at least one metal from the group consisting of molybdenum, tungsten and vanadium and at least one metal from the group consisting of nickel and cobalt, sulfur, and, usually, residual oil are oxygen pressure leached at a temperature of at least about 400.degree. F. with a base from the group consisting of sodium hydroxide and sodium aluminte in at least stoichimetric amount to yield a solution having a pH between about 7 and 9 containing dissolved molybdenum, vanadium and any tungsten which may be recovered and a readily filterable residue containing aluminum, nickel and cobalt which may be worked up to recover the valuable constituents, with overall processing being accomplished in an environmentally acceptable manner.
The process for treating spent catalyst containing aluminum, molybdenum, vanadium, sulfur and at least one metal from the group consisting of nickel and cobalt with up to 30%, by weight, oil, to recover the constituents thereof which comprises the steps of:
The process for treating an oily, spent hydrodesulfurization catalyst containing aluminum, at least one metal from the group consisting of molybdenum, vanadium and tungsten, at least one metal from the group consisting of nickel and cobalt, and sulfur which comprises forming an aqueous slurry by mixing said catalyst with an aqueous solution containing an amount of a base from the group consisting of sodium hydroxide and sodium aluminate stoichiometrically at least equivalent to convert in the presence of oxygen, the molybdenum, tungsten, vanadium and sulfur contents of said spent catalyst to sodium molybdate, sodium tungstate, sodium vanadate and sodium sulfate, oxygen pressure leaching the resulting slurry at a temperature of at least about 350.degree. F. for a time sufficient to oxidize to carbon dioxide substantially all the oil in said spent catalyst to oxidize to sodium sulfate substantially all the sulfur in said spent catalyst, and to dissolve molybdenum, tungsten and vanadium while producing a solid containing the aluminum, nickel and cobalt, discharging the products of said oxygen pressure leach at a pH not exceeding about pH 9 and separating the liquid containing said metal from the group consisting of molybdenum, tungsten, and vanadium and said sulfur but less than 100 ppm aluminum from said solid.
Dependencies are inferred from the claim text.