Methanation of carbon monoxide over tungsten carbide-containing catalysts

Claim 2

A process for producing methane comprising contacting a feed stream comprising carbon monoxide and hydrogen under methanation conditions with a catalyzing amount of a tungsten carbide-containing alumina gel 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 in said alumina gel catalyst are such that the resulting material will catalyze the conversion of carbon monoxide and hydrogen to methane.

Claim 3

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

Claim 4

A process according to claim 2 wherein the feed stream is contacted with said catalyst at a temperature in the range of about 200° C. to about 600° C. and at a pressure in the range of about 0 to about 12,000 psig.

Claim 5

A process according to claim 3 wherein the powdered tungsten carbide particles have average particle diameters in the range of 10 to about 100 micrometers.

Claim 6

A process according to claim 4 wherein the volumetric ratio of hydrogen to carbon monoxide in said feed stream is about 3.

Claim 7

A process according to claim 5 wherein the weight ratio of tungsten carbide to alumina in said catalyst is about 50/50 and said feed stream is contacted with said catalyst at about atmospheric pressure.

Claim 8

A process according to claim 6 wherein the volume of feed stream per volume of said catalyst per hour is in the range of about 200 to about 10,000.

Claim 9

A process according to claim 7 wherein said catalyst is prepared by slurrying powdered tungsten carbide with an aqueous solution of aluminum nitrate, forming the hydrogel by adding a sufficient amount of ammonium hydroxide 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, and then grinding to yield particles of about 16 to about 60 mesh.

Claim 10

A process according to claim 8 wherein said catalyst includes at least one promoter metal selected from the group consisting of ruthenium, rhodium, palladium, osmium, iridium, platinum, and rhenium and the total amount of 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 gel catalyst.

Claim 11

A process according to claim 9 wherein said promoter metal is added to the ground tungsten carbide-containing alumina gel in the form of an aqueous solution of an inorganic compound of said promotor metal, the thus-treated alumina gel is then dried, and prior to use is calcined for about 2 hours at about 500° C. under flowing hydrogen.

Claim 12

A process according to claim 9 wherein the powdered tungsten carbide-containing alumina gel is impregnated with a sufficient amount of platinum diaminodinitrite to provide about 0.15 weight percent platinum based on the weight of the unpromoted dried tungsten carbide-containing alumina gel.

Claim 13

A process according to claim 10 wherein the powdered tungsten carbide-containing alumina gel is impregnated with a sufficient amount of palladium nitrate to provide about 0.15 weight percent palladium based on the weight of the unpromoted dried tungsten carbide-containing alumina gel.

Claim 14

A process according to claim 10 wherein the powdered tungsten carbide-containing alumina gel is impregnated with a sufficient amount of perrhenic acid to provide about 0.15 weight percent rhenium based on the weight of the unpromoted dried tungsten carbide-containing alumina gel.

Claim 15

A process according to claim 4 wherein said catalyst includes at least one promoter metal selected from the group consisting of ruthenium, rhodium, palladium, osmium, iridium, platinum, and rhenium and the total amount of 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 gel catalyst.

Claim 16

A process according to claim 14 wherein the promoter metal is platinum.

Claim 17

A process according to claim 14 wherein the promoter metal is palladium.

Claim 18

A process according to claim 14 wherein the promoter metal is rhenium.

Claim 19

A process according to claim 14 wherein said catalyst consists essentially of alumina, tungsten carbide, and at least one promoter selected from the group consisting of platinum, palladium, and rhenium.

Claim 20

A process according to claim 4 wherein said catalyst consists essentially of alumina and tungsten carbide.

Claim 21

A process according to claim 4 wherein the substantial distribution of powdered tungsten carbide in alumina is provided by precipitating the alumina hydrogel from a stirred solution containing the tungsten carbide.

Claim 22

A process for producing methane comprising contacting a feed stream comprising carbon monoxide and hydrogen under methanation conditions with a catalyzing amount of tungsten carbide-containing alumina gel catalyst, said catalyst being a weight ratio of tungsten carbide to alumina in the range of about 1/99 to about 80/20 and being promoted with about 0.05 to about 5 weight percent, based on the weight of the promoted carbide-containing alumina gel catalyst, of a promoter consisting of ruthenium, rhodium, palladium, osmium, iridium, platinum, or mixtures thereof, said tungsten carbide-containing alumina gel catalyst being in the form of particles of about 16 to about 60 mesh size and having been prepared according to the steps comprising (1) mixing powdered tungsten carbide in an alumina hydrogel to obtain a substantial distribution of said tungsten carbide in said hydrogel, (2) washing the thus-obtained hydrogel with water to remove soluble impurities, (3) drying the thus-washed hydrogel to remove free water and yield an alumina gel, (4) calcining the thus-obtained alumina gel under a nonoxidizing atmosphere at a temperature in the range of about 425° C. to about 650° C. for about 2 to about 10 hours, (5) cooling the thus-calcined alumina gel, and (6) pulverizing the thus-cooled calcined alumina gel to yield particles of about 16 to about 60 mesh size.

Claim 23

A process for producing methane comprising contacting a feed stream comprising carbon monoxide and hydrogen under methanation conditions with a catalyzing amount of tungsten carbide-containing alumina gel catalyst, said catalyst being a weight ratio of tungsten carbide to alumina in the range of about 1/99 to about 80/20 and being promoted with about 0.05 to about 5 weight percent, based on the weight of the promoted carbide-containing alumina gel catalyst, of a promoter consisting of ruthenium, rhodium, palladium, osmium, iridium, platinum, or mixtures thereof, said tungsten carbide-containing alumina gel catalyst being in the form of particles of about 16 to about 60 mesh size and having been prepared according to the steps comprising (1) mixing powdered tungsten carbide in an alumina hydrogel to obtain a substantial distribution of said tungsten carbide in said hydrogel, (2) washing the thus-obtained hydrogel with water to remove soluble impurities, (3) drying the thus-washed hydrogel to remove free water and yield an alumina gel, (4) calcining the thus-obtained alumina gel under a nonoxidizing atmosphere at a temperature in the range of about 425° C. to about 650° C. for about 2 to about 10 hours, (5) cooling the thus-calcined alumina gel, and (6) pulverizing the thus-cooled calcined alumina gel to yield particles of about 16 to about 60 mesh size.

Claim 24

A process according to claim 21 wherein said tungsten carbide-containing alumina gel catalyst is one in which the promoter was added by impregnating the pulverized tungsten carbide-containing alumina gel with an aqueous solution of a sufficient amount of one or more inorganic compounds of ruthenium, rhodium, palladium, iridium, or platinum, and the impregnated alumina gel was again dried, and prior to use the alumina gel was calcined for about 2 hours at about 500° C. under a non-oxidizing atmosphere.

Claim 25

A process according to claim 22 wherein said tungsten carbide-containing alumina gel catalyst is one in which the pulverized tungsten carbide-containing alumina gel has been impregnated with a sufficient amount of platinum diaminodinitrite to provide about 0.15 weight percent platinum based on the weight of the unpromoted tungsten carbide-containing alumina gel.

Claim 26

A process according to claim 23 wherein the volumetric ratio of hydrogen to carbon monoxide in said feedstream is about 3, the feedstream is contacted with said catalyst at a temperature in the range of about 200° C. to about 600° C. and at a pressure of about 0 to about 12,000 psig, and the volume of the feedstream contacting said catalyst per volume of said catalyst per hour is in the range of about 200 to about 10,000.

Claim 27

A process according to claim 24 wherein the weight ratio of tungsten carbide to alumina in said catalyst is about 50/50.

Claim 28

A process according to claim 25 wherein said catalyst is prepared by slurrying powdered tungsten carbide with an aqueous solution of aluminum nitrite, adding a sufficient amount of ammonium hydroxide to give a pH of about 8 to form the hydrogel, filtering the hydrogel, washing the hydrogel, drying the hydrogel at about 125° C., and calcining the dried hydrogel under flowing hydrogen at a temperature of about 500° C. for about 2 hours.

Claim 29

A process according to claim 22 wherein said tungsten carbide-containing alumina gel catalyst is one in which the pulverized tungsten carbide-containing alumina gel has been impregnated with a sufficient amount of palladium nitrite to provide about 0.15 weight percent palladium based on the weight of the unpromoted tungsten carbide-containing alumina gel.

Claim 30

A process according to claim 27 wherein the volumetric ratio of hydrogen to carbon monoxide in said feedstream is about 3, the feedstream is contacted with said catalyst at a temperature in the range of about 200° C. to about 600° C. and at a pressure of about 0 to about 12,000 psig, and the volume of the feedstream contacting said catalyst per volume of said catalyst per hour is in the range of about 200 to about 10,000.

Claim 31

A process according to claim 28 wherein the weight ratio of tungsten carbide to alumina in said catalyst is about 50/50.

Claim 32

A process according to claim 29 wherein said catalyst is prepared by slurrying powdered tungsten carbide and with an aqueous solution of aluminum nitrite, adding a sufficient amount of ammonium hydroxide to give a pH of about 8 to form the hydrogel, filtering the hydrogel, washing the hydrogel, drying the hydrogel at about 125° C., and calcining the dried hydrogel under flowing hydrogen at a temperature of about 500° C. for about 2 hours.

Claim 33

A process according to claim 21 wherein the powdered tungsten carbide particles have an average particle diameter in the range of 10 to about 100 micrometers, and said promoter consists of platinum or palladium.

Claim 34

A process according to claim 31 wherein the weight ratio of tungsten carbide to alumina in said catalyst is about 50/50.

Claim 35

A process according to claim 32 wherein the volumetric ratio of hydrogen to carbon monoxide in said feedstream is about 3, the feedstream is contacted with said catalyst at a temperature in the range of about 200° C. to about 600° C. and at a pressure of about 0 to about 12,000 psig, and the volume of the feedstream contacting said catalyst per volume of said catalyst per hour is in the range of about 200 to about 10,000.