Method and device for producing a synthesis gas containing H2 and CO
AssigneeLurgi GmbH
InventorsDaniel Mateos-Queiruga, Ulrich Wolf
Life of this patent
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Abstract
In a process for producing synthesis gas by catalytic conversion of hydrocarbons contained in a desulfurized feed gas stream with steam, the mixture of feed gas and steam is preheated by heat exchange at a pressure of 10 to 45 bar to a temperature of 300 to 700° C. and is subsequently heated by heat exchange above a catalyst at a pressure of 10 to 45 bar to a temperature of 650 to 950° C. To minimize the apparatus involved, it is provided that the mixture of feed gas and steam traverses a catalyst bed contained in a reaction tank, and the catalyst bed is heated by thermal radiation and convection.
Claims3
An apparatus for performing the method for producing gas containing H2 and CO by catalytic conversion of hydrocarbons contained in a feed gas stream with steam, in that the feed gas heated to 300 to 400° C. and subsequently desulfurized is mixed with steam, the mixture of feed gas and steam is preheated by heat exchange at a pressure of 10 to 45 bar to a temperature of 300 to 700° C., and is subsequently heated over a catalyst by heat exchange at a pressure of 10 to 45 bar to a temperature of 650 to 950° C., wherein a catalyst bed contained in a vertical reaction tank is traversed by the mixture of feed gas and steam and is indirectly heated by thermal radiation and convection, wherein the vertical reaction tank includes a tube bundle comprising axially parallel, internally heatable radiant tubes closed at the bottom, in each radiant tube a flame tube concentrically is inserted by forming an annular space, said flame tube comprising apertures located in a middle section of the flame tube, and in each flame tube a gas lance concentrically is inserted by forming an annular space, and a reaction space to be traversed by the mixture of feed gas and steam is filled with a catalyst bed around the radiant tubes, wherein the reaction space of the reaction tank is filled with a catalyst bed up to a height of 30 to 75% of the overall height of the tube bundle.
Dependencies are inferred from the claim text.