Catalytic conversion of methane to higher hydrocarbons

Claim 2

A process for making higher hydrocarbons from methane comprising contacting methane with oxygen or an oxygen-containing gas in the presence of: a catalyst comprising (a) at least one metal in the elemental state of Group IB of the Periodic Table of the Elements, with the proviso that if the metal is copper an additional Group IB metal must also be present; (b) a metal-containing chloride or a metal-containing compound formed in-situ into a metal-containing chloride, said metal of said metal-containing chloride or said metal-containing compound formed in-situ into a metal-containing chloride selected from the group consisting of manganese, an alkali metal, an alkaline earth metal and a rear earth metal of the lanthanide series; and (c) a volatile halide.

Claim 3

A process in accordance with claim 1 wherein said metal of Group IB is selected from the group consisting of silver, gold, a mixture of silver and gold, a mixture of silver and copper, a mixture of gold and copper, a mixture of silver, gold and copper, an alloy of silver an gold, an alloy of silver and copper, an alloy of gold and copper, an alloy of silver, gold and copper and mixtures thereof.

Claim 4

A process in accordance with claim 2 wherein said Group IB metal is selected from the group consisting of silver, a mixture of silver and copper and an alloy of silver and copper.

Claim 5

A process in accordance with claim 3 wherein said Group IB metal is silver.

Claim 6

A process in accordance with claim 1 wherein said metal of said metal-containing chloride whether directly provided or formed from a metal-containing compound in situ is an alkali metal or an alkaline earth metal.

Claim 7

A process in accordance with claim 5 wherein said metal-containing chloride is selected from the group consisting of sodium chloride and strontium chloride.

Claim 8

A process in accordance with claim 6 wherein said metal-containing chloride is strontium chloride.

Claim 9

A process in accordance with claim 6 wherein said metal-containing chloride is sodium chloride.

Claim 10

A process in accordance with claim 1 wherein said volatile halide is selected from the group consisting of hydrogen halides, halogen gases, halide-substituted methanes and mixtures thereof.

Claim 11

A process in accordance with claim 9 wherein said volatile halide is selected from the group consisting of hydrogen halides and halide-substituted methanes.

Claim 12

A process in accordance with claim 10 wherein said volatile halide is carbon tetrachloride.

Claim 13

A process in accordance with claim 10 wherein said volatile halide is hydrogen chloride.

Claim 14

A process in accordance with claim 10 wherein said volatile halide is methyl chloride.

Claim 15

A process in accordance with claim 1 wherein said process is conducted at a temperature in the range of between about 650° C. and about 1,000° C. and at a pressure in the range of between atmospheric and about 1,000 psi.

Claim 16

A process in accordance with claim 14 wherein said process occurs at a temperature of between about 700° C. and about 900° C. and at a pressure of between atmospheric and about 700 psi.

Claim 17

A process in accordance with claim 15 wherein said process occurs at a temperature of about 725° C. to about 850° C. and at a pressure of atmospheric to about 500 psi.

Claim 18

A process in accordance with claim 16 wherein said process occurs at a temperature in the range of between about 735° C. and about 825° C. and at a pressure in the range of between atmospheric and about 250 psi.

Claim 19

A process in accordance with claim. 1 wherein said Group IB metal and said metal-containing chloride or said metal-containing compound formed into a metal-containing chloride in situ are deposited upon a carrier.

Claim 20

A process in accordance with claim 18 wherein said carrier is selected from the group consisting of silica, alumina, silicon carbide, titania, zirconia and naturally occurring materials which incorporate one or more of any of the above materials.

Claim 21

A process for making higher hydrocarbons from methane comprising contacting methane with oxygen or an oxygen-containing gas at a temperature in the range of between about 650° C. and about 1,000° C. and a pressure in the range of between about atmospheric and about 1,000 psi in the presence of a catalyst comprising: (a) at least one metal in the elemental in the elemental state of Group IB of the Periodic Table of the Elements, with the proviso that if the metal is copper an additional Group IB metal must also be present; (b) a metal-containing chloride or a metal-containing compound formed in-situ into a metal-containing chloride, said metal of said metal-containing chloride or said metal-containing compound formed in-situ into a metal-containing chloride selected from the group consisting of manganese, an alkali metal and an alkaline earth metal; and (c) a volatile halide selected from the group consisting of hydrogen halides and halide substituted methanes.

Claim 22

A process for making higher hydrocarbons from methane comprising contacting methane with oxygen or an oxygen-containing gas at a temperature in the range of between about 650° C. and about 1,000° C. and a pressure in the range of between about atmospheric and about 1,000 psi in the presence of a catalyst comprising: (a) at least one metal in the elemental in the elemental state of Group IB of the Periodic Table of the Elements, with the proviso that if the metal is copper an additional Group IB metal must also be present; (b) a metal-containing chloride or a metal-containing compound formed in-situ into a metal-containing chloride, said metal of said metal-containing chloride or said metal-containing compound formed in-situ into a metal-containing chloride selected from the group consisting of manganese, an alkali metal and an alkaline earth metal; and (c) a volatile halide selected from the group consisting of hydrogen halides and halide substituted methanes.

Claim 23

A process in accordance with claim 20 wherein said Group IB metal is silver, said metal-containing chloride whether directly provided or formed in-situ from a metal-containing compound is selected from the group consisting of sodium chloride and strontium chloride and said volatile halide is selected from the group consisting of hydrogen chloride, methyl chloride and carbon tetrachloride, said process occurring at a temperature in the range of between about 700° C. and about 850° C. and a pressure in the range of between atmospheric and about 700 psi.

Claim 24

A process in accordance with claim 21 wherein said metal-containing chloride is sodium chloride and said volatile halide is methyl chloride, said process occurring at a temperature in the range of between about 725° C. and 850° C. and at a pressure of between atmospheric and about 500 psi.

Claim 25

A process in accordance with claim 20 wherein said Group IB metal and said metal-containing chloride or metal-containing compound formed into a metal-containing chloride in situ is disposed on a carrier.

Claim 26

A process in accordance with claim 23 wherein said carrier is selected from the group consisting of silica, alumina, silicon carbide, titania, zirconia and naturally occurring materials which incorporate one or more of the above inert materials.

Claim 27

A process in accordance with claim 24 wherein said carrier is selected from the group consisting of pumice, alumina and silicon carbide.

Claim 28

A process for making higher hydrocarbons from methane comprising contacting methane with a gaseous stream of oxygen or an oxygen-containing gas and a volatile halide in the presence of a catalyst formed by the steps comprising: (a) depositing silver nitrate and strontium nitrate on a carrier selected from the group consisting of alumina, silicon carbide and pumice; and (b) hydrogenating said deposited silver nitrate and strontium nitrate.

Claim 29

A process for making higher hydrocarbons from methane comprising contacting methane with a gaseous stream of oxygen or an oxygen-containing gas and a volatile halide in the presence of a catalyst formed by the steps comprising: (a) depositing silver nitrate and strontium nitrate on a carrier selected from the group consisting of alumina, silicon carbide and pumice; and (b) hydrogenating said deposited silver nitrate and strontium nitrate.

Claim 30

A process in accordance with claim 26 wherein said volatile halide is present in a concentration of between about 0.25 mole % and about 1.2 mole %, said concentration based on the total molar concentration of said gaseous reactants and said volatile halide.

Claim 31

A process in accordance with claim 27 wherein said volatile halide is hydrogen chloride.