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1.发明申请公开(公告)号：US20150126629A1
公开(公告)日：2015-05-07
申请号：US14597240
申请日：2015-01-15
发明人： Yilong CHEN , Pingyu KUAI , Yan GONG , Xiaodong ZHAN , Yanfeng ZHANG , Jiaqi JIN
CPC分类号： C01B3/16 , C01B3/34 , C01B2203/0233 , C01B2203/0283 , C01B2203/04 , C01B2203/0445 , C01B2203/047 , C01B2203/0475 , C01B2203/062 , C01B2203/0805 , C01B2203/0827 , C01B2203/1241 , C01B2203/142 , C01B2203/84 , C07C1/0485 , C07C4/06 , C07C2523/755 , C10G2/00 , C10G2/30 , C10G2/332 , C10K1/005 , C10K3/04 , C10K3/06 , Y02P20/121
摘要： A method for recycling exhaust gas from Fischer-Tropsch synthesis. The method includes: 1) introducing raw gas to a shift reactor to conduct a water-gas shift reaction, and collecting shift gas; 2) introducing the shift gas to a Fischer-Tropsch synthesis device to yield a hydrocarbon fuel and exhaust gas, returning part of the exhaust gas as recycle gas; 3) introducing another part of the exhaust gas to a methanation reactor, allowing a methanation reaction to happen between the part of the exhaust gas and water vapor; 4) introducing a mixed gas product from the methanation reaction to a methane reforming reactor; 5) transporting the hydrogen and carbon monoxide resulting from the methane reforming reaction to a gas separator, separating the hydrogen and obtaining a mixed gas including carbon dioxide; and 6) returning the mixed gas including carbon dioxide to the methane reforming reactor.
摘要翻译： 一种从费 - 托合成回收废气的方法。 该方法包括：1）将原料气引入变换反应器进行水煤气变换反应，并收集排气; 2）将转移气体引入费 - 托合成装置以产生烃燃料和废气，使一部分排气作为循环气体返回; 3）将另一部分排气引入甲烷化反应器，使排气与水汽之间发生甲烷化反应; 4）将来自甲烷化反应的混合气体产物引入甲烷重整反应器; 5）将由甲烷重整反应产生的氢气和一氧化碳输送到气体分离器，分离氢气并获得包括二氧化碳的混合气体; 和6）将包括二氧化碳的混合气体返回到甲烷重整反应器。
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公开(公告)号：US20150099814A1
公开(公告)日：2015-04-09
申请号：US14569774
申请日：2014-12-14
发明人： Yilong CHEN , Kan SONG , Pingyu KUAI , Yan GONG , Yanfeng ZHANG , Jiaqi JIN
IPC分类号： C10G2/00
CPC分类号： C10G2/32 , C01B2203/0475 , C01B2203/0495 , C01B2203/062 , C10G2300/1011 , C10J3/00 , C10J2300/0916 , C10J2300/1618 , C10J2300/1659 , C10K1/002 , C10K3/00 , Y02E50/32 , Y02P20/145 , Y02P30/20 , Y02T50/678
摘要： A method for preparing a liquid hydrocarbon from syngas. The method includes: 1) mixing crude syngas from a biomass gasifier and a hydrogen-rich gas to yield a mixed gas; 2) dehydrating and decarbonizing the mixed gas for removal of moisture, carbon dioxide, and impurities, to yield a fine syngas; 3) introducing the fine syngas to a Fischer-Tropsch synthesis device in the presence of a catalyst, controlling a reaction temperature of the Fischer-Tropsch synthesis at between 150 and 300° C. and a reaction pressure of between 2 and 4 MPa (A), to yield a liquid hydrocarbon and water which is discharged out of the Fischer-Tropsch synthesis device; and 4) returning 70-95 vol. % of exhaust gases from the Fischer-Tropsch synthesis device to step 3) to mix with the fine syngas, and introducing the resulting mixed gas to the Fischer-Tropsch synthesis device.
摘要翻译： 从合成气制备液态烃的方法。 该方法包括：1）从生物质气化炉和富氢气体混合粗合成气，得到混合气体; 2）将混合气体脱水脱碳以除去水分，二氧化碳和杂质，产生细小的合成气; 3）在催化剂存在下将细合成气引入费 - 托合成装置中，在150-300℃之间控制费 - 托合成的反应温度和2-4MPa的反应压力（A ），以产生从费 - 托合成装置排出的液体烃和水; 和4）返回70-95卷。 从费 - 托合成装置到步骤3）的废气的％）与细合成气混合，并将所得混合气体引入费 - 托合成装置。
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3.发明申请公开(公告)号：US20190193064A1
公开(公告)日：2019-06-27
申请号：US16288063
申请日：2019-02-27
发明人： Li GUO , Jiangang CHEN , Yanfeng ZHANG , Jiaqi JIN , Youliang SHI , Shenke ZHENG , Yan GONG
IPC分类号： B01J35/00 , C10G2/00 , B01J23/745 , B01J35/10 , B01J35/08
CPC分类号： B01J35/0006 , B01J23/745 , B01J35/0046 , B01J35/08 , B01J35/10 , B01J35/1061 , B01J37/10 , C10G2/00 , C10G2/332 , C10G2300/70
摘要： A catalyst, including silica and iron. The silica is in the form of a mesoporous spherical particle. The iron is in the form of nanoparticles evenly distributed and encapsulated in the silica. The particle size of the silica is between 140 and 160 nm, and the silica includes pores between 2 and 9 nm in diameter.
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