公开(公告)号：US09988890B2

公开(公告)日：2018-06-05

申请号：US14412963

申请日：2013-07-04

Applicant: STATOIL CANADA LIMITED

Inventor： Knut Vebjørn Grande ,  Karina Heitnes Hofstad ,  Harald Vindspoll ,  Marianne Haugan

IPC: E21B43/34 ,  C10G69/04 ,  C10G69/06 ,  C10G47/00 ,  C10G65/12 ,  C01B3/34 ,  E21B43/40 ,  C10G67/04 ,  C10J3/00 ,  C10G21/00 ,  C10K1/00 ,  C01B3/36 ,  C01B3/48 ,  E21B43/24 ,  E21B43/243 ,  C10G1/00 ,  C10G1/04 ,  C10J3/60 ,  E21B41/00 ,  E21B43/16

CPC classification number: E21B43/40 ,  C01B3/36 ,  C01B3/48 ,  C01B2203/0255 ,  C01B2203/0283 ,  C01B2203/0415 ,  C01B2203/0475 ,  C01B2203/065 ,  C01B2203/0894 ,  C01B2203/86 ,  C10G1/002 ,  C10G1/045 ,  C10G21/003 ,  C10G67/0463 ,  C10G67/049 ,  C10G2300/4037 ,  C10G2300/4043 ,  C10G2300/42 ,  C10J3/00 ,  C10J3/60 ,  C10J2300/0913 ,  C10J2300/0959 ,  C10J2300/1612 ,  C10J2300/1656 ,  C10J2300/1671 ,  C10J2300/1678 ,  C10J2300/1846 ,  C10K1/005 ,  E21B41/0064 ,  E21B43/164 ,  E21B43/24 ,  E21B43/2406 ,  E21B43/2408 ,  E21B43/243 ,  Y02P30/30 ,  Y02P30/446

Abstract: The present invention relates to a method and system for recovering and processing a hydrocarbon mixture from a subterranean formation. The method comprises: (i) mobilizing said hydrocarbon mixture; (ii) recovering said mobilized hydrocarbon mixture; (iii) deasphalting said recovered hydrocarbon mixture to produce deasphalted hydrocarbon and asphaltenes; (iv) gasifying said asphaltenes in a gasifier to generate hydrogen, steam and/or energy and CO2; (v) upgrading said deasphalted hydrocarbon by hydrogen addition to produce upgraded hydrocarbon; and (vi) adding a diluent to said upgraded hydrocarbon, wherein said method is at least partially self-sufficient in terms of hydrogen and diluent.

公开(公告)号：US09719038B2

公开(公告)日：2017-08-01

申请号：US14174266

申请日：2014-02-06

Applicant: MITSUBISHI HEAVY INDUSTRIES, LTD.

Inventor： Shogo Yoshida ,  Katsuhiko Yokohama ,  Keisuke Matsuo

IPC: F01K5/02 ,  C10J3/00 ,  C10J3/72 ,  C10K1/02 ,  F01K23/10 ,  F01K23/16 ,  F22B1/18

CPC classification number: C10J3/726 ,  C10J2300/093 ,  C10J2300/094 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/1653 ,  C10J2300/1678 ,  C10K1/026 ,  F01K5/02 ,  F01K23/10 ,  F01K23/16 ,  F22B1/1815 ,  Y02E20/16 ,  Y02E20/18

Abstract: A gasifier start-up method for a gasifier capable of preventing or inhibiting a temporary occurrence of black smoke when a gasifier is started-up. A gasifier start-up method for a gasifier, in which a gasifying agent and a solid carbonaceous fuel are supplied and gasified, includes a start-up burner igniting step of supplying a start-up fuel and oxygen-containing gas to a start-up burner and igniting the start-up fuel and oxygen-containing gas, under an inert atmosphere in which an inside of the gasifier around the start-up burner is filled with inert gas; and an oxygen-containing-gas supply adjusting step of adjusting the supply of the oxygen-containing gas such that combustion gas obtained after the combustion reaction of the start-up fuel and the oxygen-containing gas becomes the inert gas, which contains little oxygen.

公开(公告)号：US20170183585A1

公开(公告)日：2017-06-29

申请号：US15312915

申请日：2015-07-02

Applicant: MITSUBISHI HITACHI POWER SYSTEMS, LTD.

Inventor： Shogo YOSHIDA ,  Yoshinori KOYAMA ,  Toshiyuki YAMASHITA

IPC: C10J3/72 ,  F02C3/28 ,  F01K11/02 ,  F01K7/16 ,  F01K23/10 ,  F01D15/10 ,  F02C3/04 ,  F02C6/18

CPC classification number: C10J3/723 ,  C10J3/46 ,  C10J3/487 ,  C10J3/726 ,  C10J3/86 ,  C10J2300/093 ,  C10J2300/0953 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/0969 ,  C10J2300/1223 ,  C10J2300/1653 ,  C10J2300/1678 ,  C10K1/024 ,  C10K1/026 ,  F01D15/10 ,  F01K7/16 ,  F01K11/02 ,  F01K23/067 ,  F01K23/10 ,  F02C3/04 ,  F02C3/28 ,  F02C6/18 ,  F05D2220/32 ,  F05D2220/72 ,  F05D2220/76 ,  F05D2240/35 ,  Y02E20/16 ,  Y02E20/18

Abstract: There is provided coal gasification unit including: a coal gasifier; a char recovery unit; flare equipment; an air flow rate adjustment valve and an oxygen supply flow passage that supply oxygen-containing gas to the coal gasifier; an inert gas supply flow passage that supplies nitrogen gas to an upstream side of the char recovery unit; and a control unit that controls a supply amount of the oxygen-containing gas and a supply amount of the nitrogen gas, in which the coal gasifier has a starting burner, and in which the control unit controls the supply amount of the nitrogen gas prior to starting combustion of starting fuel by the starting burner so that an oxygen concentration of mixed gas in which combustion gas generated by combustion of the oxygen-containing gas and the starting fuel has been mixed with the nitrogen gas becomes not more than an ignition concentration.

公开(公告)号：US09388349B2

公开(公告)日：2016-07-12

申请号：US14237378

申请日：2012-08-10

Applicant: Yoshinori Koyama ,  Yasunari Shibata ,  Osamu Shinada ,  Katsuhiko Yokohama ,  Taketoshi Sakae ,  Koji Nishimura ,  Naoto Nakayama

Inventor： Yoshinori Koyama ,  Yasunari Shibata ,  Osamu Shinada ,  Katsuhiko Yokohama ,  Taketoshi Sakae ,  Koji Nishimura ,  Naoto Nakayama

IPC: C10K1/02 ,  G01F23/288 ,  C10J3/50 ,  C10J3/72

CPC classification number: C10K1/02 ,  C10J3/506 ,  C10J3/723 ,  C10J2200/156 ,  C10J2300/093 ,  C10J2300/094 ,  C10J2300/0959 ,  C10J2300/0976 ,  C10J2300/1653 ,  C10J2300/1678 ,  C10J2300/1807 ,  C10K1/026 ,  G01F23/288 ,  G01F23/2885 ,  Y02E20/18

Abstract: The present invention includes: a char feeding hopper body that feeds separated char toward a coal gasifier; a char communicating tube that communicates with a bottom portion of the char feeding hopper body and extends in a vertical axis direction; fluid gas feeding means that is provided at a bottom portion side of the char feeding hopper body and feeds fluid gas to an inside thereof; a radiation source section that emits γ-rays toward an inside of the char communicating tube in which a level of the char reaches a level H2 which is the same level as a level H1 of the char in the char feeding hopper as a result of feeding of the fluid gas; and a γ-ray detector that is provided along a vertical axis direction of the char communicating tube and detects the emitted γ-rays.

Abstract translation: 本发明包括：向煤气化器供给分离的焦炭的炭进料斗体; 与所述炭供给料斗主体的底部连通并且在纵轴方向上延伸的炭连通管; 流体气体供给装置，设置在炭供给料斗主体的底部侧，并将流体气体供给到其内部; 向焦炭连通管内部发射γ射线的辐射源部分，其中焦炭的水平达到与进料斗中焦炭的水平H1水平相同的水平H2，作为进料的结果 的流体气体; 以及沿着焦炭连通管的纵轴方向设置的γ射线检测器，检测发射的γ射线。

公开(公告)号：US20160096998A1

公开(公告)日：2016-04-07

申请号：US14863056

申请日：2015-09-23

Applicant: COMMUNITY POWER CORPORATION

Inventor： Steve Sherwood

IPC: C10G2/00 ,  C01B3/34 ,  C10G11/05 ,  C10J3/82 ,  C10G11/00

CPC classification number: C10G2/34 ,  C01B3/34 ,  C01B2203/0205 ,  C01B2203/0283 ,  C01B2203/0405 ,  C01B2203/062 ,  C10G2/332 ,  C10G11/05 ,  C10G45/64 ,  C10J3/82 ,  C10J2300/0916 ,  C10J2300/1659 ,  C10J2300/1678 ,  C10K3/04 ,  Y02E50/32 ,  Y02T50/678

Abstract: Disclosed in the application include systems and processes for producing a liquid transportation fuel product using a carbon-containing feedstock. Also disclosed include catalysts that can be used in the systems and the processes, and processes of making the catalysts.

Abstract translation: 在本申请中公开了包括使用含碳原料生产液体运输燃料产品的系统和方法。 还公开了包括可用于体系和方法的催化剂，以及制备催化剂的方法。

公开(公告)号：US20160053992A1

公开(公告)日：2016-02-25

申请号：US14780385

申请日：2014-03-27

Applicant: JFE ENGINEERING CORPORATION

Inventor： Satoshi Horiuchi ,  Keiichi Okuyama ,  Takeshi Uchiyama ,  Hajime Akiyama ,  Junya Watanabe ,  Takashi Nakayama ,  Kazumasa Wakimoto ,  Akio Shimomura

IPC: F23G5/50 ,  F23G5/24 ,  F23L7/00 ,  F23G5/027

CPC classification number: F23G5/50 ,  C10J3/08 ,  C10J3/20 ,  C10J3/723 ,  C10J2300/0946 ,  C10J2300/0956 ,  C10J2300/1606 ,  C10J2300/1634 ,  C10J2300/1671 ,  C10J2300/1678 ,  C10J2300/1846 ,  F23G5/027 ,  F23G5/24 ,  F23G2200/00 ,  F23G2201/701 ,  F23G2202/20 ,  F23G2204/101 ,  F23G2204/103 ,  F23L7/007 ,  Y02E20/344

Abstract: Problem to be SolvedTo provide a waste gasification melting apparatus which, even if a fuel gas is used as an alternative to a part of the coke, the temperature of the coke bed can be sufficiently raised, and a method using the same.SolutionA waste gasification melting apparatus including an oxygen rich air supply apparatus 14 for blowing oxygen rich air into a tuyere 5, and a fuel gas supply apparatus 15 for supplying a fuel gas to the tuyere 5, and a controller 16 for controlling the oxygen rich air supply apparatus 14; the oxygen rich air supply apparatus 14 mixing air and oxygen to prepare oxygen rich air and supply the oxygen rich air to the tuyere 5; and the controller 16 controlling the amount of air to be mixed and the amount of oxygen to be mixed in the oxygen rich air supply apparatus 14 so as to give an oxygen concentration of the oxygen rich air in accordance with the amount of fuel gas supplied to the tuyere 5 from the fuel gas supply apparatus 15.

Abstract translation: 要解决的问题为了提供一种废气化熔化装置，即使使用燃料气体作为焦炭的一部分的替代物，也可以充分提高焦炭床的温度，以及使用其的方法。 方案一种废气化熔化装置，包括用于将富氧空气吹入风口5的富氧空气供应装置14和用于向风口5供应燃料气体的燃料气体供应装置15以及用于控制富氧的控制器16 供气装置14; 富氧空气供给装置14混合空气和氧气以制备富氧空气并将富氧空气供给到风口5; 并且控制器16控制要混合的空气量和在富氧空气供应装置14中混合的氧气的量，以便根据供给到的富氧空气的量来提供富氧空气的氧浓度 来自燃料气体供给装置15的风口5。

公开(公告)号：US09238208B2

公开(公告)日：2016-01-19

申请号：US14371367

申请日：2013-02-08

Applicant: MITSUBISHI HEAVY INDUSTRIES, LTD.

Inventor： Yoshio Seiki ,  Shuji Fujii ,  Koji Higashino ,  Kaori Yoshida ,  Masaki Yushima

IPC: B01J8/04 ,  B01J8/00 ,  B01J8/02 ,  C10K1/00 ,  C10K3/04 ,  C01B3/16 ,  B01J19/00 ,  B01J19/24 ,  C10K3/02 ,  C10K3/00 ,  C01B3/02 ,  C01B3/06 ,  C01B3/12 ,  C10J3/46

CPC classification number: B01J8/005 ,  B01J8/0278 ,  B01J8/0457 ,  B01J8/0492 ,  B01J2208/00061 ,  B01J2208/00548 ,  B01J2219/002 ,  B01J2219/00213 ,  B01J2219/00231 ,  C01B3/16 ,  C01B2203/0283 ,  C01B2203/0415 ,  C01B2203/0465 ,  C01B2203/0485 ,  C01B2203/146 ,  C10J3/466 ,  C10J2300/093 ,  C10J2300/0959 ,  C10J2300/1653 ,  C10J2300/1678 ,  C10K1/003 ,  C10K3/04 ,  Y02E20/16 ,  Y02E20/18 ,  Y02E60/36

Abstract: A CO shift reaction apparatus 11 according to the present invention includes: adiabatic reactors 31A to 31C, each having CO shift catalyst layers 35A to 35C filled with a CO shift catalyst 34 which reforms CO in gasification gas 15; gas supply lines l11 to l15 which supply the gasification gas 15 to the adiabatic reactors 31A to 31C; first gas flow rate control units 32A and 32B which adjust the amounts of gas supplied to the adiabatic reactors 31A to 31C; gas discharge lines l21 to l25 which discharge processing gas; and second gas flow rate control unit 33A and 33B which adjust flow rates of processing gas 38A-1, 38A-2, 38B-1, and 38B-2.

Abstract translation: 根据本发明的CO转换反应装置11包括：绝热反应器31A至31C，其各自具有填充有气化气体15中的CO的CO变换催化剂34的CO变换催化剂层35A至35C; 将气化气体15供应到绝热反应器31A至31C的气体供应管线111-115; 第一气体流量控制单元32A和32B，其调节供应到绝热反应器31A至31C的气体量; 排气处理气体排气管线l21〜l25; 以及调节处理气体38A-1,38A-2,38B-1和38B-2的流量的第二气体流量控制单元33A和33B。

公开(公告)号：US09228740B2

公开(公告)日：2016-01-05

申请号：US14155726

申请日：2014-01-15

Applicant: General Electric Company

Inventor： John Saunders Stevenson ,  Robert Michael Zirin ,  Raymond Douglas Steele ,  Constantin Bugescu ,  Roger Ma ,  David R. Matthews ,  Kenneth M. Sprouse

IPC: B05B1/00 ,  F23D11/38 ,  F02C3/20 ,  F02C3/22 ,  F02C3/28 ,  F02C9/40 ,  C10J3/50 ,  C10K1/16 ,  F23L7/00 ,  F23C6/04 ,  F23D1/00 ,  B01F5/02 ,  B05B1/06

CPC classification number: F23D11/38 ,  B01F5/0262 ,  B05B1/06 ,  C10J3/506 ,  C10J2200/152 ,  C10J2300/165 ,  C10J2300/1653 ,  C10J2300/1675 ,  C10J2300/1678 ,  C10K1/165 ,  F02C3/20 ,  F02C3/22 ,  F02C3/28 ,  F02C9/40 ,  F23C6/045 ,  F23C2201/20 ,  F23D1/005 ,  F23D2201/10 ,  F23D2213/00 ,  F23D2214/00 ,  F23D2900/00006 ,  F23L7/005 ,  F23L2900/07002 ,  Y02E20/16 ,  Y02E20/18 ,  Y10T29/49229 ,  Y10T29/49904

Abstract: An annular injector is described. The injector includes a first bayonet assembly and a second bayonet assembly each including a terminal end and a tip end. The second bayonet assembly is configured to be concentrically coupled at least partially about the first bayonet assembly. An outer diameter of the first bayonet assembly and an inner diameter of the second bayonet assembly vary at the tip end to define a first substantially annular nozzle. The first bayonet assembly includes a maximum outer diameter that is greater than a minimum inner diameter of the second bayonet assembly and at least a portion of at least one of the first bayonet assembly and the second bayonet assembly extends from the tip end to the terminal end. The injector includes a third bayonet assembly configured to be concentrically coupled at least partially about the second bayonet assembly to define a second substantially annular nozzle.

Abstract translation: 描述了环形注射器。 喷射器包括第一卡口组件和第二卡口组件，每个卡口组件包括终端和末端。 第二卡口组件构造成至少部分地围绕第一卡口组件同心耦合。 第一卡口组件的外径和第二卡口组件的内径在尖端处变化以限定第一基本上环形的喷嘴。 第一卡口组件包括大于第二卡口组件的最小内径的最大外径，并且第一卡口组件和第二卡口组件中的至少一个的至少一部分从尖端延伸到终端 。 喷射器包括第三卡口组件，其被配置为至少部分地围绕第二卡口组件同心联接以限定第二基本上环形的喷嘴。

公开(公告)号：US09200221B2

公开(公告)日：2015-12-01

申请号：US13284842

申请日：2011-10-28

Applicant: Gary Daniel Miller

Inventor： Gary Daniel Miller

IPC: B01J20/00 ,  C10J3/30 ,  C10J3/50 ,  C10K1/00 ,  C10K1/10

CPC classification number: C10J3/30 ,  C10J3/506 ,  C10J2300/0969 ,  C10J2300/1678 ,  C10J2300/1815 ,  C10K1/003 ,  C10K1/004 ,  C10K1/005 ,  C10K1/10 ,  Y02C10/08 ,  Y02P20/52

Abstract: Present embodiments include systems and methods for reducing variations in a solid feed provided to a gasifier. For example, in an embodiment, a gasification feed vessel includes a solid fuel inlet configured to receive a solid fuel into the gasification feed vessel, a dry mixer configured to dry mix the solid fuel within the feed vessel, a solid fuel outlet configured to deliver a feed of the solid fuel to a gasification system, and a metering device coupled to the solid fuel outlet. The metering device is configured to control an amount of the feed of the solid fuel delivered to the gasification system. The gasification feed vessel is configured to provide the feed of the solid fuel to the gasification system within a desired energy concentration range over time.

Abstract translation: 现有实施例包括用于减少提供给气化器的固体进料的变化的系统和方法。 例如，在一个实施方案中，气化进料容器包括固体燃料入口，该固体燃料入口构造成将固体燃料接收到气化进料容器中，干燥混合器构造成干燥混合进料容器内的固体燃料，固体燃料出口， 固体燃料进料到气化系统，以及连接到固体燃料出口的计量装置。 计量装置被配置为控制输送到气化系统的固体燃料的进料量。 气化进料容器被配置成在随着时间的期望的能量浓度范围内向气化系统提供固体燃料的进料。

公开(公告)号：US09157042B2

公开(公告)日：2015-10-13

申请号：US13663902

申请日：2012-10-30

Applicant: Kellogg Brown & Root LLC

Inventor： Siva Ariyapadi ,  Philip Shires

IPC: C10J3/00 ,  C10J3/56 ,  C10L3/08 ,  C10J3/48 ,  C10K1/00 ,  C10K1/02 ,  C10K1/04 ,  C10K3/04 ,  C10G2/00 ,  C10K3/00

CPC classification number: C10L3/08 ,  C10G2/30 ,  C10G2300/1022 ,  C10G2300/207 ,  C10J3/00 ,  C10J3/482 ,  C10J3/56 ,  C10J2300/093 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/0973 ,  C10J2300/0983 ,  C10J2300/1662 ,  C10J2300/1671 ,  C10J2300/1675 ,  C10J2300/1678 ,  C10J2300/1687 ,  C10J2300/1884 ,  C10J2300/1892 ,  C10K1/002 ,  C10K1/004 ,  C10K1/005 ,  C10K1/02 ,  C10K1/04 ,  C10K3/008 ,  C10K3/04

Abstract: Systems and methods for producing synthetic gas are provided. The method can include gasifying a feedstock within a gasifier to provide a raw syngas. The raw syngas can be processed within a purification system to provide a treated syngas, and the purification system can include a flash gas separator. The treated syngas and a first heat transfer medium can be converted into a synthetic gas, a second heat transfer medium, and a methanation condensate. The methanation condensate can be introduced to the flash gas separator.

Abstract translation: 提供了制造合成气体的系统和方法。 该方法可以包括在气化器内气化原料以提供原始合成气。 原料合成气可以在净化系统内处理以提供经处理的合成气，并且净化系统可以包括闪蒸气体分离器。 经处理的合成气和第一传热介质可以转化为合成气体，第二传热介质和甲烷化冷凝物。 甲烷化冷凝物可以引入闪蒸气分离器。