Composition control of gases
AssigneeBritish Gas Corporation
InventorsBrian Hoyle Thompson, Henry Lawrence Conway
Life of this patent
Estimating the term…
Abstract
Gases which are produced by the hydrogenolysis of hydrocarbons and which contain hydrogen, paraffins and aromatic compounds are contacted with a quenching medium such as a cooled fluidised bed or a cooled inert gas or liquid to cool the gas to a temperature lower than that which will support any substantial reaction between the hydrogen, paraffinic and aromatic constituents to produce carbonaceous compounds which will be deposited on the surfaces of reaction vessel or gas off-takes. Methane containing gases produced by the non-catalytic hydrogenolysis of oils with a hydrogenating gas at temperatures between 500.degree.-1000.degree.C may be quenched to a temperature not greater than 700.degree.C to prevent after reaction.
Claims13
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.
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.degree. to 1000.degree.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.degree.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.
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.degree. to 750.degree.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.degree.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.
Dependencies are inferred from the claim text.