US2007215520A1PendingUtilityA1
Method for Conversion of Hydrocarbons
Est. expiryNov 21, 2023(expired)· nominal 20-yr term from priority
C01B 3/38C01B 3/26C01B 2203/047B82Y 30/00D01F 9/133Y02E60/32C01B 2203/0277D01F 9/1272C01B 2203/0405C01B 2203/1047C01B 2203/0475C01B 3/505C01B 2203/048C01B 2203/1241D01F 9/127D01F 9/1271
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Claims
Abstract
The invention provides a method for the conversion into carbon of gaseous hydrocarbons extracted from a natural hydrocarbon reservoir, which method comprises contacting said gaseous hydrocarbon at an elevated temperature in a reactor with a catalyst capable of converting said hydrocarbon to carbon and hydrogen; burning hydrogen produced by the conversion of the hydrocarbon, optionally after separating hydrogen produced from unconverted hydrocarbon, burning said hydrogen to generate energy; and using the energy generated to heat said reactor or the gaseous hydrocarbon flow thereto, or to heat or power a heat or power consuming apparatus.
Claims
exact text as granted — not AI-modified1 . A method for the conversion into carbon of gaseous hydrocarbons extracted from a natural hydrocarbon reservoir, which method comprises contacting said gaseous hydrocarbon at an elevated temperature in a reactor with a catalyst capable of converting said hydrocarbon to carbon and hydrogen; separating hydrogen produced from unconverted hydrocarbon; burning said hydrogen to generate energy; and using the energy generated to heat said reactor or the gaseous hydrocarbon flow thereto, or to heat or power a heat or power consuming apparatus.
2 . A method as claimed in claim 1 wherein the energy generated is used to heat said reactor or the gaseous hydrocarbon flow thereto.
3 . A method as claimed in claim 1 wherein the energy generated is used to power an electricity generator.
4 . A method as claimed in claim 1 wherein said catalyst is particulate.
5 . A method as claimed in claim 1 wherein said catalyst is a Raney metal.
6 . A method as claimed in claim 1 wherein said catalyst comprises an element selected from Ni, Co and Fe.
7 . A method as claimed in claim 1 wherein said catalyst is particulate with a mode particle size of 1 to 300 μm.
8 . A method as claimed in claim 1 wherein hydrogen is burned in an internal combustion engine.
9 . A method as claimed in claim 1 wherein the hydrogen is separated from the unconverted hydrocarbon using a hydrogen-permeable membrane.
10 . An apparatus for the conversion of hydrocarbon gas to carbon, said apparatus comprising a reactor vessel ( 2 ) having a gas inlet port ( 18 ) and a gas outlet port ( 19 );
a separator ( 4 ) for removing hydrogen from a hydrocarbon and hydrogen containing gas; a gas conduit ( 3 ) from said gas outlet port to said separator; a combustor ( 9 ) arranged to burn hydrogen from said separator to generate energy; and an energy transferrer ( 11 ) arranged to transfer energy from said combustor to said reactor vessel or to a further heat or power consuming apparatus ( 20 ).
11 . An apparatus as claimed in claim 9 further comprising an electricity generator ( 20 ) powered by energy from said combustor.
12 . A process for the preparation of fibrous carbon which comprises contacting a metallic catalyst with a carbon-containing gas at elevated temperature, characterized in that said catalyst is sponge iron.Cited by (0)
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