Conversions of low molecular weight hydrocarbons to higher molecular weight hydrocarbons using a metal compound-containing catalyst (II-A)

Claim 2

A process for the production of higher molecular weight hydrocarbons from lower molecular hydrocarbons comprising the steps of: (a) introducing into a reaction zone a lower molecular weight hydrocarbon-containing gas and contacting said gas in said zone with a metal compound-containing catalyst containing a carbide, nitride, boride or oxide of a Group II-A metal, under C 2 + hydrocarbon synthesis conditions such that at least 15 mole percent of the lower molecular weight hydrocarbons in said gas are converted to higher molecular weight hydrocarbons, said conditions including a temperature of greater than 1000° C. and a gas hourly spaced velocity of greater than 6000 hr -1 ; (b) withdrawing from said reaction zone a higher molecular weight hydrocarbon-containing stream.

Claim 3

The process of claim 1 wherein said temperature is in the range of 1100 to 1200° C., said space velocity is in the range of greater than 6,000 to 36,000 hr -1 and at least 20 mole percent of said lower molecular weight hydrocarbons are converted to higher molecular weight hydrocarbons.

Claim 4

The process of claim 2 wherein said reaction zone contains a stationary or fluidized bed of a catalyst.

Claim 5

The process of claim 3 wherein said lower molecular weight hydrocarbon is methane.

Claim 6

The process of claim 4 wherein said temperature is in the range of 1140° to 1175° C. and said space velocity is in the range of 9,000 to 18,000 hr -1 .

Claim 7

The process of claim 5 wherein 40 or more mole percent of said methane containing hydrocarbon gas is converted to higher molecular weight hydrocarbons.

Claim 8

The process of claim 6 wherein said higher molecular weight hydrocarbon is rich in ethylene or aromatics or both.

Claim 9

A process for the production of higher molecular weight hydrocarbons from methane comprising the steps of: (a) introducing into a reaction zone a methane-containing gas and contacting said gas in said zone with a catalyst containing a carbide, nitride, boride or oxide of a Group II-A metal selected from beryllium, magnesium, calcium, strontium, barium or radium under C 2 + hydrocarbon synthesis conditions such that at least 20 mole percent of said methane in said gas is converted to higher molecular weight hydrocarbons, said conditions including a temperature in the range of 1100° to 1200° C. and a gas hourly space velocity of 6,000 to 36,000 hr -1 ; and (b) withdrawing from said reaction zone a higher molecular weight hydrocarbon-containing stream, wherein the carbon-containing reaction products in said stream comprises greater than 90 mole percent higher molecular weight hydrocarbons.

Claim 10

A process for the production of higher molecular weight hydrocarbons from methane comprising the steps of: (a) introducing into a reaction zone a methane-containing gas and contacting said gas in said zone with a catalyst containing a carbide, nitride, boride or oxide of a Group II-A metal selected from beryllium, magnesium, calcium, strontium, barium or radium under C 2 + hydrocarbon synthesis conditions such that at least 20 mole percent of said methane in said gas is converted to higher molecular weight hydrocarbons, said conditions including a temperature in the range of 1100° to 1200° C. and a gas hourly space velocity of 6,000 to 36,000 hr -1 ; and (b) withdrawing from said reaction zone a higher molecular weight hydrocarbon-containing stream, wherein the carbon-containing reaction products in said stream comprises greater than 90 mole percent higher molecular weight hydrocarbons.

Claim 11

The process of claim 8 wherein at least 20 mole percent of said lower molecular weight hydrocarbons are converted to higher molecular weight hydrocarbons.

Claim 12

The process of claim 9 wherein said reaction zone contains a stationary or fluidized bed of a catalyst.

Claim 13

The process of claim 10 wherein said lower molecular weight hydrocarbon is methane.

Claim 14

The process of claim 11 wherein said temperature is in the range of 1140° to 1175° C. and said space velocity is in the range of 9,000 to 18,000 hr -1 .

Claim 15

The process of claim 12 wherein 40 or more mole percent of said methane containing hydrocarbon gas is converted to higher molecular weight hydrocarbons.

Claim 16

The process of claim 13 wherein said higher molecular weight hydrocarbon stream is rich in ethylene or aromatics or both.

Claim 17

A process for the production of higher molecular weight hydrocarbons from methane comprising the steps of: (a) introducing into a reaction zone a methane-containing gas and contacting said gas in said zone with a catalyst containing calcium oxide or magnesium oxide under C 2 + hydrocarbon synthesis conditions such that at least 20 mole percent of said methane in said gas is converted to higher molecular weight hydrocarbons, said conditions including a temperature in the range of 1100° to 1200° C. and a gas hourly space velocity of 6,000 to 36,000 hr -1 ; and (b) withdrawing from said reaction zone a higher molecular weight hydrocarbon-containing stream, wherein the carbon-containing reaction products in said stream comprises greater than 80 mole percent higher molecular weight hydrocarbons.

Claim 18

A process for the production of higher molecular weight hydrocarbons from methane comprising the steps of: (a) introducing into a reaction zone a methane-containing gas and contacting said gas in said zone with a catalyst containing calcium oxide or magnesium oxide under C 2 + hydrocarbon synthesis conditions such that at least 20 mole percent of said methane in said gas is converted to higher molecular weight hydrocarbons, said conditions including a temperature in the range of 1100° to 1200° C. and a gas hourly space velocity of 6,000 to 36,000 hr -1 ; and (b) withdrawing from said reaction zone a higher molecular weight hydrocarbon-containing stream, wherein the carbon-containing reaction products in said stream comprises greater than 80 mole percent higher molecular weight hydrocarbons.