Process for the production of substitute natural gas
AssigneeThe Ralph M. Parsons Company
InventorsGerald A. White, Theodore R. Roszkowski
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AssigneeThe Ralph M. Parsons Company
InventorsGerald A. White, Theodore R. Roszkowski
Estimating the term…
There is provided a process for the production of substitute natural gas (SNG) from carbonaceous materials such as hydrocarbon liquids including hydrocarbon fractions and/or solid carbonaceous fuels, by non-catalytic partial oxidation of the carbonaceous materials in the presence of process generated oxygen and high pressure steam, to form a gas stream containing principally hydrogen and oxides of carbon which are suitable for catalytic conversion to methane under conditions where sufficient waste heat is recovered in the form of high pressure steam to satisfy the steam requirements for the process and that necessary to drive compressors to produce oxygen from air as required by the partial oxidiation stage. A product gas stream containing up to 99.9% methane and less than 1 ppm sulfur compounds may be obtained. There may be included as part of the process a carburetion stage following the partial oxidation stage where intermediate hydrocarbon fractions are converted in part to methane and in part to hydrogen and the oxides of carbon.
A process for the production of substitute natural gas which comprises:
A process for the production of substitute natural gas which comprises:
In a process for the production of methane from a feed stream comprising hydrogen, the oxides of carbon and water, as steam, is contacted with a supported catalyst containing at least one metal from the third period of Group VIII of the Periodic Table in a wet methanation zone the improvement which comprises contacting the feed stream in the wet methanation zone with a supported catalyst which contains from about 5 to about 35% by weight of at least one metal of the third period of Group VIII of the Periodic Table on a temperature stabilized, ceramic alumina support, said support being heat treated at a temperature above the highest temperature encountered in said wet methanation zone prior to the addition of said metal thereto, said supported catalyst being capable of causing a water-gas shift reaction and methanation at a temperature from about 900.degree.F to about 1600.degree.F, to form methane at a temperature in which the feed temperature to the wet methanation zone is at least about 900.degree.F and the exit temperature is up to about 1600.degree.F, said wet methanation zone being operated to form methane under adiabatic conditions and then removing the heat of reaction following the wet methanation zone.
Dependencies are inferred from the claim text.