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公开(公告)号:US4074981A
公开(公告)日:1978-02-21
申请号:US749658
申请日:1976-12-10
Applicant: William L. Slater
Inventor: William L. Slater
CPC classification number: C10J3/86 , C01B3/22 , C01B3/36 , C10J3/485 , C10J3/74 , C10J3/78 , C10J3/84 , C10J3/845 , C10K1/101 , C10J2300/093 , C10J2300/0943 , C10J2300/0946 , C10J2300/0956 , C10J2300/0959 , C10J2300/0979 , C10J2300/1671 , C10J2300/1807 , C10J2300/1846 , C10J2300/1884 , C10J2300/1892
Abstract: A continuous process for producing simultaneously a stream of cooled clean synthesis gas, reducing gas, or fuel gas and a separate stream of superheated steam. In the subject process a hydrocarbonaceous fuel is reacted with a free-oxygen containing gas by partial oxidation in the reaction zone of a free-flow noncatalytic gas generator. The effluent gas stream from the reaction zone is quenched in water in a quench zone and further cooled by being passed serially through first and second heat exchange zones to produce a product gas stream of cooled clean synthesis gas, fuel, or reducing gas. Simultaneously, a stream of boiler feed water is converted into superheated steam by stepwise sequential indirect heat exchange with the following sources of heat: first with a stream of carbon-quench water dispersion from said quench zone, second with said effluent gas stream in said second heat exchange zone, and third with the effluent gas stream in said first heat exchange zone. Optionally, the process gas stream may be cooled further, scrubbed with water, passed through a separating zone to remove entrained water, and expanded in a gas turbine for the production of mechanical or electrical energy.
Abstract translation: 一种用于同时生产冷却的清洁合成气流,还原气体或燃料气体以及单独的过热蒸汽流的连续方法。 在本发明方法中,烃类燃料与自由流动的非催化燃气发生器的反应区中的含氧气体通过部分氧化反应。 来自反应区的废气流在骤冷区中在水中淬火,并通过串联地通过第一和第二热交换区进一步冷却,以产生冷却的清洁合成气,燃料或还原气体的产物气流。 同时,通过与以下热源的逐步顺序间接热交换将锅炉给水流转换成过热蒸汽:首先用来自所述骤冷区的碳骤冷水分散体流,其次是在所述第二个流中的所述废气流 热交换区,第三与所述第一热交换区中的废气流。 任选地,工艺气体流可以进一步冷却,用水洗涤,通过分离区以除去夹带的水,并在燃气轮机中膨胀以产生机械或电能。
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公开(公告)号:US3620700A
公开(公告)日:1971-11-16
申请号:US3620700D
申请日:1969-08-15
Applicant: WARREN G SCHLINGER , WILLIAM L SLATER , ROGER M DILLE , JOSEPH P TASSONEY
Inventor: SCHLINGER WARREN G , SLATER WILLIAM L , DILLE ROGER M , TASSONEY JOSEPH P
CPC classification number: C01B3/36 , B01D53/34 , C01B3/50 , C01B2203/049
Abstract: Free carbon soot entrained in the product gas of a free-flow synthesis gas generator is recovered in a sedimentation vessel as part of a thickened dispersion of solids in water from which clear supernatant water is easily separated by supplying particulate petroleum coke to the sedimentation vessel or to the reaction zone of said gas generator as a portion of the fuel, or by mixing the carbon soot-water dispersion in the sedimentation vessel with a thickened water slurry of unconverted petroleum coke such as produced by quenching in water the product gas of a second free-flow synthesis gas generator in which the fuel comprises raw particulate petroleum coke and the thickened underflow from said sedimentation vessel.
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