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filingDate 1961-02-28-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationDate 1964-08-19-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber GB-966882-A
titleOfInvention Hydrocarbon reforming process
abstract A process for producing hydrogen and oxides of carbon comprises reforming a hydrocarbon feed with steam at an elevated temperature in the presence of a catalyst comprising elementary or combined nickel, a refractory material and an alkaline compound, the steam to hydrocarbon ratio being at least sufficient substantially to prevent deposition of carbon on the catalyst. The hydrocarbon may be naphtha or some other liquid hydrocarbon feedstock; it may contain olefines and/or sulphur and may be reformed between 600 DEG and 1000 DEG F. at a pressure between 0 and 1000 p.s.i.g. Examples given compare the utility of conventional and novel catalysts for steam reformation of heptane, ethylene-ethane, and propylene-propane mixtures. Specification 966,883 is referred to.ALSO:A process for producing hydrogen and oxides of carbon comprises reforming a hydrocarbon feed with steam at an elevated temperature in the presence of a catalyst comprising elementary or combined nickel, a refractory material and an alkaline compound, the steam-to-hydrocarbon ratio being at least sufficient substantially to prevent deposition of carbon on the catalyst. The hydrocarbon may be naphtha or some other liquid hydrocarbon feedstock; it may contain olefines and/or sulphur and may be reformed between 600 DEG and 1000 DEG F. at a pressure between 0 and 1000 p.s.i.g. Examples are given in which conventional and novel catalysts are compared for the steam reformation of (1) n-heptane, (2) ethylene-ethane mixture, and (3) propylene-propane mixture. Specification 966,883 is referred to.ALSO:A steam reforming hydrocarbon catalyst comprises elementary or combined nickel, a refractory material and an alkaline metal compound, the steam-to-hydrocarbon ratio being at least sufficient substantially to prevent deposition of carbon on the catalyst. The nickel may be present as NiO and may form 4-40% of the catalyst. The alkaline compound may be a hydroxide, carbonate, bicarbonate, nitrate, sulphate, silicate, oxalate or acetate of Na, K, Li or Ca and Mg. The refractory oxide may be an alumino silicate, calcium silicate, silica, zirconia, magnesia or alumina. Specification 966,883 is referred to.
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priorityDate 1960-03-01-04:00^^<http://www.w3.org/2001/XMLSchema#date>
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