Composition control of gases

Claim 2

A process for controlling the composition of gases produced by the hydrogenolysis of carbonaceous fuels which process comprises contacting said gas in a vessel with a quenching medium to cool the gas to a temperature lower than that which will support substantial reactions involving any of the components hydrogen, paraffinic hydrocarbons or aromatic hydrocarbons, present in the gas, wherein said quenching is achieved by interposing a stream of insert gas between said gas and the walls of the vessel containing said gas, and admixing a cooling fluid containing a major proportion of monocyclic aromatic compounds with said gas to cool it to temperature at which any higher molecular weight constituents which would be deposited on surfaces are dissolved in said cooling fluid.

Claim 3

A process as claimed in claim 1 wherein said gas in said vessel is a methane containing gas.

Claim 4

A process as claimed in claim 1 wherein said gas in said vessel is rich in ethane.

Claim 5

A process as claimed in claim 1 wherein said inert gas is cooled product, said gas in said vessel is selected from the group consisting of a hydrogenating gas for use in the hydrogenolysis of carbonaceous fuels, carbon dioxide and steam.

Claim 6

A process as claimed in claim 1 wherein said cooling fluid comprises a benzene-rich liquid.

Claim 7

A process as claimed in claim 5 wherein said cooling fluid comprises benzole.

Claim 8

A process as claimed in claim 5 wherein said cooling fluid comprises a benzole-water mixture.

Claim 9

In a process for the production of methane by the vapor phase non-catalytic hydrogenolysis of a hydrocarbon feedstock wherein (i) the vapor of a normally liquid hydrocarbon feedstock is reacted with a hydrogen containing gas at a temperature of from 500° to 1000°C to produce a gas comprising a major proportion of methane and minor proportions of other paraffins, hydrogen carbon oxides and aromatic compounds, the improvement comprising (ii) interposing a stream of an inert gas between said methane containing gas and the walls of a vessel containing said methane containing gas, and (iii) contacting the methane containing gas with a benzene cooling fluid to cool the methane containing gas after substantial completion of the hydrogenolysis reaction to a temperature of not greater than 700°C and which is lower than that which will support substantial reaction involving any of the components selected from the group consisting of hydrogen, paraffinic hydrocarbons and aromatic hydrocarbons which are present in said methane containing gas.

Claim 10

In a process for the production of methane by the vapor phase non-catalytic hydrogenolysis of a hydrocarbon feedstock wherein (i) the vapor of a normally liquid hydrocarbon feedstock is reacted with a hydrogen containing gas at a temperature of from 500° to 1000°C to produce a gas comprising a major proportion of methane and minor proportions of other paraffins, hydrogen carbon oxides and aromatic compounds, the improvement comprising (ii) interposing a stream of an inert gas between said methane containing gas and the walls of a vessel containing said methane containing gas, and (iii) contacting the methane containing gas with a benzene cooling fluid to cool the methane containing gas after substantial completion of the hydrogenolysis reaction to a temperature of not greater than 700°C and which is lower than that which will support substantial reaction involving any of the components selected from the group consisting of hydrogen, paraffinic hydrocarbons and aromatic hydrocarbons which are present in said methane containing gas.

Claim 11

A process as claimed in claim 8 wherein said hydrogenolysis step (i) is effected by causing said feedstock and said hydrogen-containing gas to circulate in admixture along an endless path.

Claim 12

A process as claimed in claim 8 wherein said hydrogenolysis step (i) is effected within a circulating bed of fluidised solid particles which are inert with respect to the hydrogenolysis reactions.

Claim 13

In a process for the production of ethane rich gases by the non-catalytic hydrogenolysis of a hydrocarbon feedstock in the vapor phase wherein the vapor of a normally liquid hydrocarbon feedstock is reacted with a hydrogen containing gas at a temperature of from 650° to 750°C to produce a gas comprising a major proportion of methane and minor proportions of other paraffins, hydrogen, carbon oxides and aromatic compounds, the improvement comprising contacting the ethane containing gas with a quenching medium selected from the group consisting of a fluidised bed of solid particulate material, steam, water, carbon dioxide, a benzene-rich liquid, previously produced methane or ethane containing gas and a hydrogen containing gas to cool the methane containing gas after substantial completion of the hydrogenolysis reaction to a temperature of not greater than 700°C and which is lower than that which will support substantial reactions involving any of the components selected from the group consisting of hydrogen, paraffinic hydrocarbons and aromatic hydrocarbons which are present in said ethane containing gas.

Claim 14

In a process for the production of ethane rich gases by the non-catalytic hydrogenolysis of a hydrocarbon feedstock in the vapor phase wherein the vapor of a normally liquid hydrocarbon feedstock is reacted with a hydrogen containing gas at a temperature of from 650° to 750°C to produce a gas comprising a major proportion of methane and minor proportions of other paraffins, hydrogen, carbon oxides and aromatic compounds, the improvement comprising contacting the ethane containing gas with a quenching medium selected from the group consisting of a fluidised bed of solid particulate material, steam, water, carbon dioxide, a benzene-rich liquid, previously produced methane or ethane containing gas and a hydrogen containing gas to cool the methane containing gas after substantial completion of the hydrogenolysis reaction to a temperature of not greater than 700°C and which is lower than that which will support substantial reactions involving any of the components selected from the group consisting of hydrogen, paraffinic hydrocarbons and aromatic hydrocarbons which are present in said ethane containing gas.

Claim 15

A process as claimed in claim 11 wherein said hydrogenolysis step is effected by causing said feedstock and said hydrogen-containing gas, in admixture, to circulate along an endless path.

Claim 16

A process as claimed in claim 11 wherein said hydrogenolysis reaction is effected within a circulating bed of fluidised solid particles which are inert with respect to the hydrogenolysis reactions.