发明授权
US5980596A Multi-injector autothermal reforming process and apparatus for producing
synthesis gas (law 565).
失效
多喷射器自热重整工艺和合成气生产设备(法律565)。
- 专利标题: Multi-injector autothermal reforming process and apparatus for producing synthesis gas (law 565).
- 专利标题(中): 多喷射器自热重整工艺和合成气生产设备(法律565)。
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申请号: US845706申请日: 1997-04-25
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公开(公告)号: US5980596A公开(公告)日: 1999-11-09
- 发明人: Frank Hershkowitz , Harry W. Deckman , Robert P. Reynolds , Constantine P. Gonatas , John W. Fulton , Leonard Schoenman , Jack I. Ito , Russell J. Koveal , Costas A. Coulaloglou
- 申请人: Frank Hershkowitz , Harry W. Deckman , Robert P. Reynolds , Constantine P. Gonatas , John W. Fulton , Leonard Schoenman , Jack I. Ito , Russell J. Koveal , Costas A. Coulaloglou
- 申请人地址: NJ Florham Park
- 专利权人: Exxon Research and Engineering Co.
- 当前专利权人: Exxon Research and Engineering Co.
- 当前专利权人地址: NJ Florham Park
- 主分类号: B01F5/00
- IPC分类号: B01F5/00 ; B01F5/06 ; B01J4/00 ; B01J8/02 ; B01J19/24 ; C01B3/36 ; C01B3/38 ; C10G2/00 ; F23D14/22 ; F23D14/62 ; B01J8/00 ; B01J8/04 ; C07C27/00
摘要:
A novel injector/reactor apparatus and an efficient process for the partial oxidation of light hydrocarbon gases, such as methane, to convert such gases to useful synthesis gas for subsequent hydrocarbon synthesis. Sources of a light hydrocarbon gas, such as methane, and oxygen or an oxygen-containing gas are preheated and pressurized and injected through an injector means at high velocity into admixture with each other in the desired proportions, preferably at comparable momentums, at a plurality of mixing nozzles which are open to the reaction zone of a reactor and are spaced over the face of the injector, to form a reactant gas premix having a pressure drop equal to at least 1% of the lowest upstream pressure of either of said gas streams. The gas premix is ejected in a time period which preferably is less than 9 milliseconds, at a velocity between about 25 to 1000 feet/second, into a reaction zone comprising a partial oxidation zone, so that the gas mixture reacts therein. The partially-oxidized effluent is then passed into a steam reforming catalyst zone to reduce the amounts of CO.sub.2, H.sub.2 O and heat produced by the partial oxidation reaction to form the useful syngas, which is cooled, recovered and/or further processed.
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