초록 ▼

The endothermic reaction of a hydrocarbon feedstock with steam and/or carbon dioxide is carried out using a double-tube reactor. In one preferred form of the reactor the catalyst is present as a coating on the outside of the inner tube. In another form inner tubes are mounted in one tube-plate and t

The endothermic reaction of a hydrocarbon feedstock with steam and/or carbon dioxide is carried out using a double-tube reactor. In one preferred form of the reactor the catalyst is present as a coating on the outside of the inner tube. In another form inner tubes are mounted in one tube-plate and the outer tubes in a second tube plate and the tube plates are disposed across a cylindrical shell so as to define a heat exchange zone (provided with a heat source) a reactants feed zone and a products offtake zone. The heat source is preferably a burner, to be fed with the product of the endothermic reaction, followed by a secondary reforming catalyst. The apparatus makes possible processes for making raw hydrogen-containing gases with advantageous internal heat recovery.

대표청구항 ▼

1. A process for producing a hydrogen-containing gas stream comprising the steps of a) feeding a reactants mixture of a hydrocarbon feedstock and steam into a plenum zone; b) passing hot gas through a plurality of first tubes, each of which has a portion extending through said plenum zone and an

1. A process for producing a hydrogen-containing gas stream comprising the steps of a) feeding a reactants mixture of a hydrocarbon feedstock and steam into a plenum zone; b) passing hot gas through a plurality of first tubes, each of which has a portion extending through said plenum zone and an inlet portion outside said plenum zone, and effecting heat exchange in said plenum zone between said hot gas and said reactants mixture thereby forming a heated reactants mixture; c) feeding the heated reactants mixture from said plenum zone into externally heated annular zones located in a heat exchange zone, each of said annular zones being associated with one of said first tubes and defined by the inlet portion of the associated first tube; and a second tube extending from the plenum zone and surrounding the inlet portion of the associated first tube, each of said second tubes being closed at the end thereof remote from said plenum zone; d) reacting said heated reactants mixture in said annular zones over a first catalyst disposed within said annular zones to produce reformed gas containing carbon oxides, hydrogen, methane, and steam; e) feeding the reformed gas from each annular zone into the inlet portion of the first tube defining that annular zone, and through the inlet portion of that first tube in heat exchange with the heated reactants mixture undergoing reaction in the annular zone and then through the portion of that first tube extending through said plenum zone as said hot gas in heat exchange with the reactants mixture in the plenum zone, thereby partly cooling said reformed gas; f) collecting the partly cooled reformed gas from said first tubes in a products offtake zone, feeding the partly cooled reformed gas to a burner, partially combusting it with an oxygen-containing gas selected from the group consisting of oxygen, air, and oxygen-enriched air and passing the combustion products over a second catalyst whereby to decrease the methane content thereof; and g) passing the effluent from said second catalyst past the exteriors of the second tubes whereby to provide the external heating of the annular zones. 2. A process according to claim 1 wherein said burner and second catalyst are disposed within said heat exchange zone but upstream of the closed ends of the second tubes.