Autothermal production of synthesis gas

• US 4,666,680 A
• Filed: 01/30/1984
• Issued: 05/19/1987
• Est. Priority Date: 01/30/1984
• Status: Expired due to Term

• Current Assignee: Fluor Corporation
• Original Assignee: Fluor Corporation
• Inventors: Lewis, Jerry L.
• Primary Examiner(s): Lacey, David L.
• Assistant Examiner(s): Johnson, William R.
• Application Number:
  US06/574,921
• Time in Patent Office: 1,205 Days
• Field of Search: 422/148, 422/197, 422/312, 422/193, 422/191, 423/360-362, 518/706, 518/715, 252/373
• US Class Current: 422/628
• CPC Class Codes: B01J 8/06 in tube reactors; the solid particles being arranged in tubes
• CPC Class Codes: C01B 2203/0233 the reforming step being a steam reforming step
• CPC Class Codes: C01B 2203/0244 the reforming step being an autothermal reforming step, e.g. secondary reforming processes
• CPC Class Codes: C01B 2203/06 Integration with other chemical processes
• CPC Class Codes: C01B 2203/061 Methanol production
• CPC Class Codes: C01B 2203/062 Hydrocarbon production, e.g. Fischer-Tropsch process
• CPC Class Codes: C01B 2203/068 Ammonia synthesis
• CPC Class Codes: C01B 2203/0844 the non-combustive exothermic reaction being another reforming reaction as defined in groups C01B2203/02 - C01B2203/0294
• CPC Class Codes: C01B 2203/0883 by indirect heat exchange
• CPC Class Codes: C01B 2203/1011 Packed bed of catalytic structures, e.g. particles, packing elements
• CPC Class Codes: C01B 2203/1052 Nickel or cobalt catalysts
• CPC Class Codes: C01B 2203/1241 Natural gas or methane
• CPC Class Codes: C01B 2203/143 Three or more reforming, decomposition or partial oxidation steps in series
• CPC Class Codes: C01B 2203/1604 Starting up the process
• CPC Class Codes: C01B 2203/82 Several process steps of C01B2203/02 - C01B2203/08 integrated into a single apparatus
• CPC Class Codes: C01B 3/025 Preparation or purification of gas mixtures for ammonia synthesis
• CPC Class Codes: C01B 3/384 the catalyst being continuously externally heated

Abstract

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.

Claims

1. 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.

2. The reactor of claim 1 further comprises flow baffles which are positioned within the first portion of said heat-exchange chamber to direct the flow of combustion reaction effluent about said reaction tubes.

3. The reactor of claim 1 in which said means communicating with said reaction tubes is a collector positioned adjacent the outlet end of said reaction tubes with a pipe extending vertically downward therefrom through said partition and into said combustion chamber.

4. The reactor of claim 1 further comprising suspension means for attaching said plurality of reaction tubes to said reactor.