Abstract A process is provided whereby carbon oxides and hydrogen in a gaseous mixture that also contains hydrocarbons are caused to react over a catalyst with the production of methane in such manner that any ethane present in the reactants is virtually unaffected by the methanation reactions. The catalyst may comprise nickel or colbalt associated with alumina, silica, magnesia, chromia or urania, or mixtures thereof. The process may be operated, in relation to the catalyst, within a range of temperatures and pressures such that hydrogenation of the carbon oxides present in the gas is substantially completed at an upper temperature limit while ethane present in the gas remains substantially unreacted at the said upper limit.
A method for the production of a fuel gas by methanation of a gas comprising contacting a gas produced by the hydrogenation of liquid hydrocarbon feedstocks with a hydrogenation gas at high temperature, said gas containing methane, ethane, carbon monoxide, carbon dioxide, and hydrogen, with a hydrogenation catalyst selected from the group consisting of nickel-alumina-silica, nickel magnesia, nickel-chromia, nickel-urania-alumina, nickel silica and cobalt silica at elevated pressure and at an elevated temperature such that hydrogenation of carbon oxides present in the reactants is substantially complete at a temperature below that necessary for the hydrogenation of ethane.
Claim 2
Independent Claim
96 words
A method for the production of a fuel gas by methanation of a gas comprising contacting a gas produced by the hydrogenation of liquid hydrocarbon feedstocks with a hydrogenation gas at high temperature, said gas containing methane, ethane, carbon monoxide, carbon dioxide, and hydrogen, with a hydrogenation catalyst selected from the group consisting of nickel-alumina-silica, nickel magnesia, nickel-chromia, nickel-urania-alumina, nickel silica and cobalt silica at elevated pressure and at an elevated temperature such that hydrogenation of carbon oxides present in the reactants is substantially complete at a temperature below that necessary for the hydrogenation of ethane.
Claim 3
Dependent Claim
14 words
A method according to claim 1 wherein said catalyst is a nickel-chromia hydrogenation catalyst.