Methanation of carbon monoxide over tungsten carbide-containing alumina catalyst for methanation of carbon monoxide

Claim 2

A tungsten carbide-containing alumina catalyst produced by mixing powdered tungsten carbide in an alumina hydrogel to obtain a substantial distribution of said tungsten carbide in said hydrogel, washing the hydrogel with water to remove soluble impurities, drying the hydrogel to remove free water, and then calcining the dried hydrogel under a nonoxidizing atmosphere, wherein the amounts of alumina and tungsten carbide are such that the resulting catalyst will catalyze the conversion of carbon monoxide and hydrogen to methane.

Claim 3

A catalyst according to claim 1 wherein the weight ratio of tungsten carbide to alumina is in the range of about 1/99 to about 80/20.

Claim 4

A catalyst according to claim 2 wherein the average particle diameter of the particles of said powdered tungsten carbide is in the range of about 10 to about 100 micrometers.

Claim 5

A catalyst according to claim 3 which is promoted with at least one promoter metal selected from the group consisting of ruthenium, rhodium, palladium, osmium, iridium, platinum, and rhenium and the total amount of said promoter metal is in the range of about 0.05 to about 5 weight percent, based on the weight of the promoted dried tungsten carbide-containing alumina.

Claim 6

A catalyst according to claim 4 wherein said promoter metal is platinum.

Claim 7

A catalyst according to claim 4 wherein said promoter metal is palladium.

Claim 8

A catalyst according to claim 4 wherein said promoter metal is rhenium.

Claim 9

A catalyst according to claim 4 wherein said catalyst is prepared by slurrying powdered tungsten carbide with an aqueous solution of aluminum nitrate, forming the alumina hydrogel while stirring said slurry by adding a sufficient amount of ammonium hydroxide to said slurry to give a pH of about 8, filtering the hydrogel, washing the hydrogel, drying the hydrogel at about 125° C., calcining the dried hydrogel under flowing hydrogen at a temperature of about 500° C. for about 2 hours, then grinding the calcined product to yield particles of about 16 to about 60 mesh.

Claim 10

A catalyst according to claim 8 wherein said promoter metal is added to the ground tungsten carbide-containing alumina in the form of an aqueous solution of a suitable inorganic compound of said promoter metal, then the treated alumina is dried, and then the dried alumina is calcined for about two hours at about 500° C. under flowing hydrogen.

Claim 11

A catalyst according to claim 9 prepared by impregnating the ground tungsten carbide-containing alumina with a sufficient amount of platinum diaminodinitrite to provide about 0.15 weight percent platinum based on the weight of the unpromoted ground tungsten carbide-containing alumina.

Claim 12

A catalyst according to claim 9 prepared by impregnating the ground tungsten carbide-containing alumina with a sufficient amount of palladium nitrate to provide about 0.15 weight percent palladium based on the weight of the unpromoted ground tungsten carbide-containing alumina.

Claim 13

A catalyst according to claim 9 prepared by impregnating the ground tungsten carbide-containing alumina with a sufficient amount of perrhenic acid to provide about 0.15 weight percent rhenium based on the weight of the unpromoted ground tungsten carbide-containing alumina.

Claim 14

A catalyst according to claim 9 prepared by impregnating the ground tungsten carbide-containing alumina with a sufficient amount of perrhenic acid to provide about 0.15 weight percent rhenium based on the weight of the unpromoted ground tungsten carbide-containing alumina.

Claim 15

A catalyst according to claim 3 wherein said catalyst is prepared by slurrying powdered tungsten carbide with an aqueous solution of aluminum nitrate, forming the alumina hydrogel while stirring said slurry by adding a sufficient amount of ammonium hydroxide to said slurry to give a pH of about 8, filtering the hydrogel, washing the hydrogel, drying the hydrogel at about 125° C., calcining the dried hydrogel under flowing hydrogen at a temperature of about 500° C. for about 2 hours, then grinding the calcined product to yield particles of about 16 to about 60 mesh.