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    COMBUSTION BURNER AND PRESSURIZED GASIFICATION FURNACE
    31.
    发明申请
    COMBUSTION BURNER AND PRESSURIZED GASIFICATION FURNACE 审中-公开
    燃烧器和加压气化炉

    公开(公告)号：US20150345788A1

    公开(公告)日：2015-12-03

    申请号：US14654681

    申请日：2013-11-28

    Applicant: MITSUBISHI HEAVY INDUSTRIES, LTD.

    Inventor： Yasuyuki MIYATA ,  Yasuo SODA ,  Katsuhiko YOKOHAMA ,  Shinya HAMASAKI ,  Keisuke MATSUO

    IPC: F23Q9/00 ,  F23D14/02

    CPC classification number: F23Q9/00 ,  C10J3/487 ,  C10J3/726 ,  C10J2200/152 ,  C10J2300/093 ,  C10J2300/0989 ,  F23C5/32 ,  F23D14/02 ,  F23D14/70 ,  F23D2207/00

    Abstract: A combustion burner and a pressurized gasification furnace provided with: a burner main body (41) capable of blowing a fuel gas in which fuel and air are mixed; and an ignition torch (42) that is provided inside the burner main body (41) and propagates a flame from the base end part of the torch, with the flame being discharged from the tip end part. By arranging the tip end part (42a) of the ignition torch (42) at the base-end side with respect to the tip end part (41a) of the burner main body (41), the thermal load at the tip end part of the ignition torch during ignition is reduced, and thus the durability can be improved.

    Abstract translation: 一种燃烧器和加压气化炉，具有：燃烧器主体（41），能够吹入混合有燃料和空气的燃料气体; 和点火炬（42），其设置在燃烧器主体（41）的内部，并从火炬的基端部传播火焰，火焰从前端部排出。 通过将点火炬（42）的前端部（42a）相对于燃烧器主体（41）的前端部（41a）设置在基端侧，将前端部的热负荷 点火时的点火炬减少，耐久性提高。

    Top-feeding double-swirl type gasifier
    32.
    发明授权
    Top-feeding double-swirl type gasifier 有权
    顶馈双旋式气化炉

    公开(公告)号：US09170018B2

    公开(公告)日：2015-10-27

    申请号：US13514116

    申请日：2010-12-10

    Applicant: Jin Wook Lee ,  Seok Woo Chung ,  Young Don Yoo ,  Yongseung Yun ,  Sam Ryong Park ,  Gyoo Tae Kim ,  Yong Il Lee

    Inventor： Jin Wook Lee ,  Seok Woo Chung ,  Young Don Yoo ,  Yongseung Yun ,  Sam Ryong Park ,  Gyoo Tae Kim ,  Yong Il Lee

    IPC: C10J1/207 ,  F23D1/00 ,  C10J3/48 ,  C10J3/50 ,  C10J3/52

    CPC classification number: F23D1/00 ,  C10J3/485 ,  C10J3/487 ,  C10J3/506 ,  C10J3/526 ,  C10J2200/152 ,  C10J2300/0906 ,  C10J2300/093 ,  Y02E20/18

    Abstract: The present invention provides a top-feeding double-swirl type gasifier: a feed line through which pulverized coal is supplied by nitrogen; a distributor for dividing the pulverized coal supplied; a plurality of burner nozzles for supplying the pulverized coal, divided in the distributor, and an oxidizer; a pressure reactor in which the pulverized coal and the oxidizer react with each other to produce a flow of synthesis gas; and a swirl generator for imparting a swirling force to the oxidizer which is fed into the pressure reactor, the gasifier further comprising a slag cooling and storing container placed beneath the pressure reactor. Each of the burner nozzles consists of a triple tube having a circular cross section. The pulverized coal and carrier gas are supplied to the most central region of the burner nozzle, and an oxidizer is supplied to an annular region 34 surrounding the central region.

    Abstract translation: 本发明提供一种顶部进料双涡流式气化器：通过氮气供给粉煤的进料管线; 分配供应的粉煤的分销商; 用于供给分配在分配器中的粉煤的多个燃烧器喷嘴和氧化剂; 其中粉煤和氧化剂彼此反应以产生合成气流的压力反应器; 以及用于向进入压力反应器的氧化剂施加旋转力的涡旋发生器，气化器还包括置于压力反应器下方的炉渣冷却和储存容器。 每个燃烧器喷嘴由具有圆形横截面的三重管组成。 粉煤和载气被供应到燃烧器喷嘴的最中心区域，并且将氧化剂供应到围绕中心区域的环形区域34。

    Cyclonic reactor with non-equilibrium gliding discharge and plasma process for reforming of solid hydrocarbons
    34.
    发明授权
    Cyclonic reactor with non-equilibrium gliding discharge and plasma process for reforming of solid hydrocarbons 有权
    具有非平衡滑行排放的旋风反应器和固体烃重整的等离子体方法

    公开(公告)号：US08864953B2

    公开(公告)日：2014-10-21

    申请号：US14060941

    申请日：2013-10-23

    Applicant: Drexel University

    Inventor： Alexander F. Gutsol ,  Alexander Fridman ,  Anatoliy Polevich ,  Michael J. Gallagher

    IPC: B01J19/08

    CPC classification number: C01B3/26 ,  C10J3/18 ,  C10J3/487 ,  C10J2300/0916 ,  C10J2300/092 ,  C10J2300/093 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/0973 ,  C10J2300/1238 ,  Y02P20/145

    Abstract: A reactor for reforming a hydrocarbon, and associated processes and systems, are described herein. In one example, a reactor is provided that is configured to use non-equilibrium gliding arc discharge plasma. In another example, the reactor uses a vortex flow pattern. Two stages of reforming are described. In a first stage, the hydrocarbon absorbs heat from the wall of the reactor and combusts to form carbon dioxide, carbon monoxide, and water. In a second stage, a gliding arc discharge is use to form syngas, which is a mixture of hydrogen gas and carbon monoxide. The heat generated by the combustion of the first stage transfers to the wall of the reactor and heated products of the second stage mix with incoming hydrocarbon to provide for partial recuperation of the reaction energy.

    Abstract translation: 本文描述了用于重整碳氢化合物的反应器以及相关联的方法和系统。 在一个示例中，提供了构造成使用非平衡滑动电弧放电等离子体的反应器。 在另一个实例中，反应器使用涡流模式。 描述了两个阶段的改造。 在第一阶段，烃从反应器壁吸收热量并燃烧形成二氧化碳，一氧化碳和水。 在第二阶段中，使用滑动电弧放电来形成合成气，其是氢气和一氧化碳的混合物。 由第一阶段的燃烧产生的热量转移到反应器的壁和第二阶段的加热产物与进入的烃混合以提供反应能量的部分回收。

    GASIFICATION DEVICE WITH SLAG REMOVAL FACILITY
    37.
    发明申请
    GASIFICATION DEVICE WITH SLAG REMOVAL FACILITY 审中-公开
    具有排渣装置的气化装置

    公开(公告)号：US20110058991A1

    公开(公告)日：2011-03-10

    申请号：US12735963

    申请日：2009-02-13

    Applicant: Eberhard Kuske ,  Christoph Hanrott

    Inventor： Eberhard Kuske ,  Christoph Hanrott

    IPC: B01J8/00

    CPC classification number: C10J3/526 ,  C10J3/485 ,  C10J3/487 ,  C10J3/76 ,  C10J3/845 ,  C10J2200/152 ,  C10K1/101

    Abstract: A device for the gasification of liquid or fine-grain solid fuel materials in an entrained bed reactor, at temperatures above the ash melting point and at a pressure of 0.3 to 8 MPa, including a gasification reactor and a water bath being arranged in a pressure vessel. The water bath being installed below the gasification reactor and the a/m gasification reactor being designed in such a manner that the synthesis gas produced is withdrawn in the upper section of the reactor, the liquid slag precipitating on the walls of the reactor chamber and then having a free downflow, without any solidification of the surface of the said slag. The lower side of the reaction chamber has an outlet opening with a drop-off edge so that the downstream of liquid slag can freely fall from the drop-off edge. A slag removal duct is arranged below the opening and reaches down into the water bath, the upper wall section of the slag removal duct is penetrated by a cooling agent and the internal side of the duct is completely lined with a temperature-resistant insulating compound. The lower section of the slag removal duct which reaches down into the water bath is wetted by a water film on the internal side, the upper and lower sections being connected with each other in such a manner that the water film of the upper wall section does not come into contact with the wall section penetrated by a cooling agent nor with the insulating compound.

    Abstract translation: 一种用于在夹带床反应器中，在高于灰熔点和0.3至8MPa的压力的温度下气化液态或细粒状固体燃料的装置，包括气化反应器和水浴，压力 船只。 安装在气化反应器下面的水浴和a / m气化反应器设计成使得所生产的合成气在反应器的上部被排出，液态渣沉淀在反应室的壁上，然后 具有自由下流，没有所述炉渣表面的任何固化。 反应室的下侧具有带有脱落边缘的出口，使得液态炉渣的下游部分可以从下落边缘自由地落下。 除渣管道布置在开口下方并向下进入水浴中，除渣管道的上壁部分被冷却剂穿透，管道的内侧完全衬有耐温绝缘化合物。 向下进入水浴的除渣管道的下部被内侧的水膜润湿，上部和下部彼此连接，使得上壁部分的水膜 不与由冷却剂渗透的壁部分或绝缘化合物接触。

    Process and apparatus for the endothermic gasification of carbon
    38.
    发明授权
    Process and apparatus for the endothermic gasification of carbon 有权
    碳吸热气化的工艺和装置

    公开(公告)号：US07776114B2

    公开(公告)日：2010-08-17

    申请号：US11460379

    申请日：2006-07-27

    Applicant: Dietmar Rüger ,  Olaf Schulze ,  Jonas Kappeller ,  Burkhard Möller ,  Bodo Max Wolf

    Inventor： Dietmar Rüger ,  Olaf Schulze ,  Jonas Kappeller ,  Burkhard Möller ,  Bodo Max Wolf

    IPC: C10J3/00

    CPC classification number: C10J3/487 ,  C10J3/526 ,  C10J3/64 ,  C10J3/84 ,  C10J2200/158 ,  C10J2300/1609

    Abstract: A process for the endothermic gasification of solid carbon in an entrained bed facility comprises partial oxidation of fuel(s) and endothermic gasification of solid carbon, preferably preceded by low temperature carbonization such that the carbonization gas is passed to the partial oxidation and the carbonization coke is passed to the endothermic gasification. The hot gas streaming downwardly from the combustion chamber is deflected to produce separation of the liquid slag and is then passed to the endothermic gasification that operates with a rising gas stream and with addition of solid carbon having a grain diameter of up to 20 mm. The speed of the gas at the carbon inlet is higher than, and the speed of the gas at the end of the endothermic gasification is lower than, the suspension rate of the reactive carbon particles, to produce an increase of the relative speed difference between the gas and the carbon particles. Apparatus is also disclosed for carrying out the process.

    Abstract translation: 在夹带床设备中固体碳的吸热气化的方法包括燃料的部分氧化和固体碳的吸热气化，优选在低温碳化之前，使得碳化气体进入部分氧化和碳化焦炭 被传递到吸热气化。 从燃烧室向下流动的热气体被偏转以产生液体炉渣的分离，然后被传递到用升高的气流运行的吸热气化，并加入具有高达20mm的粒径的固体碳。 碳入口处的气体速度高于吸热气化结束时的气体速度低于反应性碳颗粒的悬浮速度，以产生相对速度差 气体和碳颗粒。 还公开了用于执行该过程的装置。

    METHOD AND APPARATUS FOR PRODUCING SYNTHESIS GAS FROM WASTE MATERIALS
    39.
    发明申请
    METHOD AND APPARATUS FOR PRODUCING SYNTHESIS GAS FROM WASTE MATERIALS 审中-公开
    从废物中生产合成气的方法和装置

    公开(公告)号：US20100092352A1

    公开(公告)日：2010-04-15

    申请号：US12638484

    申请日：2009-12-15

    Applicant: Robert E. Klepper

    Inventor： Robert E. Klepper

    IPC: C10J3/48

    CPC classification number: C10J3/84 ,  C10J3/487 ,  C10J3/50 ,  C10J2200/15 ,  C10J2200/154 ,  C10J2200/158 ,  C10J2300/0903 ,  C10J2300/093 ,  C10J2300/0973

    Abstract: An apparatus designed to form syn gas from carbonaceous materials such as coal includes a devolatilization reactor in combination with a reformer reactor which subsequently forms syn gas. The reformer reactor, in turn, is in communication with a particulate separator. The devolatilization reactor is fed with material using a compression feeder which drives air from the feed material, compresses it in a feed zone forming a seal between the feed hopper and the devolatilization reactor. The reformer reactor, as well as the particulate separators, are maintained in a heated furnace so that the temperature of the formed syn gas does not decrease below the reaction temperature until particulate material has been separated.

    Abstract translation: 设计用于从碳质材料如煤形成合成气的设备包括与随后形成合成气的重整器反应器组合的脱挥发反应器。 重整器反应器又与颗粒分离器连通。 脱挥发反应器使用压缩进料器进料，该压缩进料器驱动来自进料的空气，并将其压缩在进料区中，形成进料斗和脱挥发反应器之间的密封。 重整器反应器以及颗粒分离器被保持在加热的炉中，使得所形成的合成气的温度不降低到反应温度以下，直到颗粒物质被分离出来。

    METHOD AND APPARATUS FOR PRODUCING METHANE FROM CARBONACEOUS MATERIAL
    40.
    发明申请
    METHOD AND APPARATUS FOR PRODUCING METHANE FROM CARBONACEOUS MATERIAL 失效
    从碳材料生产甲烷的方法和装置

    公开(公告)号：US20100024298A1

    公开(公告)日：2010-02-04

    申请号：US12543398

    申请日：2009-08-18

    Applicant: Raymond S. Hobbs

    Inventor： Raymond S. Hobbs

    IPC: C01B3/32

    CPC classification number: B01J19/2405 ,  B01J19/26 ,  B01J2219/00763 ,  C01B3/50 ,  C01B3/586 ,  C01B2203/0445 ,  C01B2203/047 ,  C01B2203/0475 ,  C01B2203/0485 ,  C10J3/487 ,  C10J3/506 ,  C10J2300/0903 ,  C10J2300/0906 ,  C10J2300/093 ,  C10J2300/0966 ,  C10J2300/0969 ,  C10J2300/1662 ,  C10J2300/1807 ,  C10K1/004 ,  C10K1/005 ,  C10K1/024 ,  C10L3/08 ,  Y02P20/133

    Abstract: A method for producing methane (69) from a carbonaceous (22) material includes conveying pulverized carbonaceous material (28) entrained in an inert carrier fluid, such as carbon dioxide (36), into a reactor (34). The reactor (34) includes a vortex region (72) for receiving hydrogen gas (38) and imparting a swirling motion to the hydrogen gas (38). The pulverized carbonaceous material (28) is exposed to the swirling stream of hydrogen gas (38) in a first reaction zone (114) within the reactor (34) to form an exit gas (40) that includes methane (69). Remaining unreacted carbonaceous material (28) is further exposed to the hydrogen gas (38) in a second, low velocity, reaction zone (120). The methane rich exit gas (40) is subsequently extracted from the reactor (34) for further processing.

    Abstract translation: 从碳质（22）材料生产甲烷（69）的方法包括将夹带在诸如二氧化碳（36）的惰性载体流体中的粉碎的碳质材料（28）输送到反应器（34）中。 反应器（34）包括用于接收氢气（38）并向氢气（38）施加漩涡运动的涡流区域（72）。 粉碎的碳质材料（28）在反应器（34）内的第一反应区（114）中暴露于氢气（38）的回旋流中以形成包括甲烷（69）的出口气体（40）。 剩余的未反应的碳质材料（28）在第二低速反应区（120）中进一步暴露于氢气（38）。 随后从反应器（34）中提取富含甲烷的出口气体（40）用于进一步处理。

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