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A process and apparatus for the auto-thermal production of hydrogen rich synthesis gas wherein a mixture of steam and a hydrocarbon feed gas is reacted by passing through a catalyst counter-currently to the flow of the combustion reaction effluent of the process. Reaction tubes are mounted within a

A process and apparatus for the auto-thermal production of hydrogen rich synthesis gas wherein a mixture of steam and a hydrocarbon feed gas is reacted by passing through a catalyst counter-currently to the flow of the combustion reaction effluent of the process. Reaction tubes are mounted within a heat exchange chamber of the reactor and are adapted to contain catalyst to effect the reaction of the mixture. Oxygen or oxygen-enriched air is introduced into a combustion chamber within the reactor to effect combustion, and the combustion reaction effluent is passed through a second catalyst zone to provide additional reaction and is thereafter passed about the exterior of the reaction tubes to effect heat exchange with the mixture passing through the tubes. The exothermic heat of reaction from combustion thus provides the heat for the endothermic reaction occurring within the reaction tubes and within the second catalyst zone.

대표청구항 ▼

An autothermal reactor for the production of a synthesis gas in which both primary reforming and secondary reforming are achieved at a high level of efficiency, comprising a heat exchange chamber having a first portion and a second portion, a first inlet connected to said heat exchange chamber for t

An autothermal reactor for the production of a synthesis gas in which both primary reforming and secondary reforming are achieved at a high level of efficiency, comprising a heat exchange chamber having a first portion and a second portion, a first inlet connected to said heat exchange chamber for the introduction of steam and feed gas to said heat exchange chamber, a plurality of reaction tubes mounted within the first portion of said heat exchanger chamber at a location spaced longitudinally from said first inlet in communication with said first inlet and in non-concentric relationship therewith so as to provide a flow path for the steam and feed gas from said first inlet through said plurality of reaction tubes, each of said plurality of reaction tubes containing catalyst therein to effect a first reforming reaction and being located in relation to said first inlet such that the flow of steam and feed gas introduced through said first inlet will be distributed amongst said plurality of reaction tubes, a combustion reaction chamber, means communicating with said reaction tubes to pass the thus reacted gases from said tubes to said combustion reaction chamber, said means extending longitudinally from said reaction tubes and extending generally into said combustion reaction chamber, a second inlet connected to said combustion reaction chamber so as to introduce oxygen or oxygen enriched air into said combustion reaction chamber, said second inlet being in non-concentric relationship with said combustion reaction chamber, means defining a second catalyst zone located in the second portion of said heat exchange chamber, a partition separating said heat exchange chamber from said combustion reaction chamber, said partition including means to permit the passage of combustion reaction effluent therethrough to said second catalyst zone, wherein said second catalyst zone comprises a catalyst bed supported on said partition to effect a second reforming reaction, whereby the combustion reaction effluent can pass through said partition and said second catalyst zone to undergo additional reforming reaction and to produce synthesis gas, an outlet for removal of synthesis gas positioned in said reactor approximately adjacent said first inlet and in non-concentric relationship with said first inlet and with said reaction tubes so that the synthesis gas passes about the outside of said reaction tubes prior to removal through said outlet which provides heat for said first reforming reaction within said reaction tubes and cools the synthesis gas.