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    Fuel gasification system
    21.
    发明授权
    Fuel gasification system 有权
    燃油气化系统

    公开(公告)号：US08747501B2

    公开(公告)日：2014-06-10

    申请号：US13683265

    申请日：2012-11-21

    申请人： IHI Corporation

    发明人： Takahiro Murakami ,  Koubun Kyo ,  Toshiyuki Suda

    IPC分类号： C10J1/207

    CPC分类号： C10J3/84 ,  C10J3/482 ,  C10J3/485 ,  C10J3/56 ,  C10J3/721 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/0973 ,  C10J2300/0993 ,  C10J2300/1671 ,  C10J2300/1807 ,  F27B15/00

    摘要： A fuel gasification system including a gasification furnace including a fluidized bed formed by fluidizing reactant gas for gasifying fuel charged into gasification gas and flammable solid content, a combustion furnace for combustion of the flammable solid content into which the flammable solid content produced in the furnace is introduced together with bed material and that includes a fluidized bed formed by fluidizing reactant gas, a material separator such as hot cyclone that separates bed material from exhaust gas introduced from the combustion furnace, the separated bed material being fed through a downcomer to the gasification furnace, and a tar decomposing mechanism that heats the gasification gas produced in the furnace to decompose tar contained in the gasification gas.

    摘要翻译： 一种燃气气化系统，包括气化炉，其包括通过使反应气体流化而形成的流化床，用于将装入气化气体的燃料气化和可燃性固体成分气化，用于燃烧在炉中产生的可燃固体成分的易燃固体成分的燃烧炉为 与床料一起引入，其包括通过使反应气体流化而形成的流化床，将床材料与从燃烧炉引入的废气分离的热旋风分离器的材料分离器，分离的床材料通过降液管进料至气化炉 以及焦化分解机构，其加热在炉中产生的气化气体，以分解气化气体中所含的焦油。

    Gasification system and method using fuel injectors
    22.
    发明授权
    Gasification system and method using fuel injectors 有权
    使用燃油喷射器的气化系统和方法

    公开(公告)号：US08696774B2

    公开(公告)日：2014-04-15

    申请号：US12684000

    申请日：2010-01-07

    申请人： Cliff Yi Guo

    发明人： Cliff Yi Guo

    IPC分类号： C10J1/207

    CPC分类号： C10J3/721 ,  C10J3/506 ,  C10J2200/152 ,  Y02E20/16 ,  Y02E20/18

    摘要： A system is provided that comprises a gasifier with an enclosure disposed about a chamber, wherein the enclosure comprises a top wall, a bottom wall, and a side wall between the top and bottom walls. The gasifier also comprises an outlet disposed in the bottom wall, a first injector disposed in the top wall, and a second injector disposed in the side wall, wherein the first and second injectors are configured to inject fuel, oxygen, or a combination thereof, into the chamber.

    摘要翻译： 提供了一种系统，其包括具有围绕室设置的封闭件的气化器，其中所述外壳包括顶壁，底壁和位于顶壁和底壁之间的侧壁。 气化器还包括设置在底壁中的出口，设置在顶壁中的第一喷射器和设置在侧壁中的第二喷射器，其中第一和第二喷射器被配置为喷射燃料，氧气或其组合， 进入房间

    Fuel reformer
    23.
    发明授权
    Fuel reformer 失效
    燃油重整器

    公开(公告)号：US08690976B2

    公开(公告)日：2014-04-08

    申请号：US12939993

    申请日：2010-11-04

    申请人： In-Hyuk Son

    发明人： In-Hyuk Son

    IPC分类号： C10J1/207 ,  B01J7/00 ,  F23D23/00

    CPC分类号： B01J8/0257 ,  B01J8/0285 ,  B01J8/0465 ,  B01J8/0496 ,  B01J2208/00504 ,  B01J2208/0053 ,  C01B3/34 ,  C01B3/48 ,  C01B2203/0233 ,  C01B2203/0283 ,  C01B2203/066 ,  C01B2203/0844 ,  C01B2203/82

    摘要： A fuel reformer is provided that is capable of improving endurance and performance. The fuel reformer includes a first burner having a first-burner first end, a first-burner second end, and a first opening formed in the first-burner first end; a second burner surrounding the first burner and having a second-burner second end, a second-burner second end, and a second opening in the second-burner first end, wherein the second-burner second end is coupled to the first-burner second end to communicate a fluid. The reforming reactor is configured to generate heat from the first and second burners, and has a fuel supply including a nozzle unit in the first burner and supplies a second oxidation fuel from the outside to the first burner. A first oxidation fuel is introduced into the first opening and flows through the first burner in a first direction and flows through the second burner in a third direction opposite to the first direction. The nozzle unit discharges the second oxidation fuel in a second direction crossing the first direction.

    摘要翻译： 提供能够提高耐久性和性能的燃料重整器。 燃料重整器包括具有第一燃烧器第一端，第一燃烧器第二端和形成在第一燃烧器第一端中的第一开口的第一燃烧器; 第二燃烧器围绕第一燃烧器并且具有第二燃烧器第二端，第二燃烧器第二端和第二燃烧器第一端中的第二开口，其中第二燃烧器第二端联接到第一燃烧器第二端 结束沟通流体。 重整反应器被配置为从第一和第二燃烧器产生热量，并且在第一燃烧器中具有包括喷嘴单元的燃料供应器，并将第二氧化燃料从外部供应到第一燃烧器。 第一氧化燃料被引入第一开口并沿着第一方向流过第一燃烧器，并沿与第一方向相反的第三方向流过第二燃烧器。 喷嘴单元沿与第一方向交叉的第二方向排出第二氧化燃料。

    Process for the gasification of carbonaceous materials
    27.
    发明授权
    Process for the gasification of carbonaceous materials 失效
    碳质材料气化工艺

    公开(公告)号：US4322222A

    公开(公告)日：1982-03-30

    申请号：US183777

    申请日：1980-09-03

    申请人： Allan Sass

    发明人： Allan Sass

    IPC分类号： C10J1/207 ,  C10J3/46 ,  C10J3/62

    CPC分类号： C10J1/207 ,  C10J3/466 ,  C10J3/485 ,  C10J3/62 ,  C10J3/721 ,  C10J3/78 ,  C10J3/84 ,  C10J2300/0909 ,  C10J2300/093 ,  C10J2300/0946 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/0969 ,  C10J2300/0976 ,  C10J2300/1659 ,  C10J2300/1662 ,  C10J2300/1807 ,  C10J2300/1823 ,  C10J2300/1884 ,  C10J2300/1892 ,  Y02E50/32

    摘要： Carbonaceous material is gasified in a first pyrolysis zone substantially in an absence of free oxygen by heating with a solid heating media. The carbonaceous material is conducted through the first pyrolysis zone in turbulent flow to provide for the rapid transfer of heat to effect the gasification.Gaseous products are recovered while char products are introduced into a second pyrolysis zone for additional gasification. The second pyrolysis zone is maintained substantially free of free oxygen. Gasification in the second pyrolysis zone is effected by the transfer of heat from a heating media to the char products produced in the first pyrolysis zone.Gaseous products from the second pyrolysis zone are recovered.The char products from the second pyrolysis zone can be heated to a temperature sufficient for use as a solid heating media.The gaseous product from the first pyrolysis zone, after separation from the char product, can be cooled to a lower temperature to condense a liquid product therefrom.Liquid products produced can be recycled to the pyrolysis zones to produce additional gaseous products. The gaseous product from the second pyrolysis zone can be used as a conveying gas for the carbonaceous feed, char products, and recycle char.A portion of the char product and the gaseous product can be converted to methane for the production of pipeline gas.

    摘要翻译： 通过用固体加热介质加热，碳质材料在基本上不存在游离氧的第一热解区中气化。 碳质材料通过湍流中的第一热解区进行，以提供快速转移热量以实现气化。 气态产物被回收，而焦炭产物被引入第二个热解区以进行另外的气化。 第二热解区基本上不含游离氧。 第二热解区中的气化通过将热量从加热介质转移到在第一热解区中产生的炭产物来实现。 回收来自第二热解区的气态产物。 可以将来自第二热解区的炭产物加热到足以用作固体加热介质的温度。 来自第一热解区的气态产物在与焦炭产物分离后可被冷却到较低温度以冷凝液体产物。 所生产的液体产品可以再循环到热解区产生额外的气态产物。 来自第二热解区的气态产物可用作碳质进料，炭产物和再循环炭的输送气体。 焦炭产物和气体产物的一部分可以转化成甲烷，用于生产管道气体。

    Pyrolysis apparatus
    28.
    发明授权
    Pyrolysis apparatus 失效
    热解设备

    公开(公告)号：US4225392A

    公开(公告)日：1980-09-30

    申请号：US939204

    申请日：1978-09-05

    申请人： Leland T. Taylor

    发明人： Leland T. Taylor

    IPC分类号： C10B1/04 ,  C10B49/08 ,  C10B53/00 ,  C10J1/207 ,  C10B9/00 ,  C10J3/20

    CPC分类号： C10J1/207 ,  C10B1/04 ,  C10B49/08 ,  C10B53/00

    摘要： A conical reaction region in a pyrolysis device has an adjustable height, adjustable speed agitator in the vicinity of the grate and a second agitator stirring the incoming material. A feed auger stops short of the reaction chamber to produce a sealing region in which the incoming feed material effectively produces a gas tight seal preventing the exit of reaction products. A gas outlet flow rate sensor controls the air inflow rate and/or lower agitator speed. Temperature and other sensors may be used to further optimize the process.

    摘要翻译： 热解装置中的锥形反应区域在炉排附近具有可调节的高度，可调节的速度搅拌器，以及搅拌进料的第二搅拌器。 进料螺旋钻停止反应室的短路以产生密封区域，在该密封区域中，进料进料有效地产生防止反应产物排出的气密密封。 气体出口流量传感器控制空气流入速率和/或较低的搅拌器速度。 温度和其他传感器可用于进一步优化过程。

    Steam gasification of coke
    29.
    发明授权
    Steam gasification of coke 失效
    焦炭的蒸汽气化

    公开(公告)号：US3803023A

    公开(公告)日：1974-04-09

    申请号：US26405672

    申请日：1972-04-19

    申请人： EXXON RESEARCH ENGINEERING CO

    发明人： HAMNER G

    IPC分类号： C10B55/10 ,  C10J1/207 ,  C10G9/32

    CPC分类号： C10J1/207 ,  C10B55/10

    摘要： A heavy carbonaceous material having a Conradson carbon residue of at least 5 wt. % is coked in the presence of an alkali metal compound to produce an active surface carbon containing the alkali metal compound. The coke is then partially gasified to produce a hydrogen-containing gas and the remaining coke is recycled to the coking zone as seed coke therein.