公开(公告)号：US09327261B2

公开(公告)日：2016-05-03

申请号：US14096313

申请日：2013-12-04

Applicant: L'Air Liquide Societe Anonyme Pour l'Etude et l'Exploitation des Procedes Georges Claude

Inventor： Taekyu Kang ,  Rong Fan ,  Pavol Pranda ,  Hwanho Kim ,  Robert A. Gagliano

IPC: B01J7/00 ,  B01J12/00 ,  C01B3/38

CPC classification number: B01J12/005 ,  C01B3/384 ,  C01B2203/0233 ,  C01B2203/0877 ,  C01B2203/1288 ,  C01B2203/1614

Abstract: An apparatus for decreasing steam methane reformer (SMR) tube temperature is provided. The apparatus can include an SMR furnace, a monitoring system in communication with the SMR furnace and a water source in fluid communication with the SMR furnace. The SMR furnace includes a plurality of SMR tubes disposed within the SMR furnace. The monitoring system is configured to monitor the temperature of at least a plurality of SMR tubes and compare the temperature against a first predetermined value, and the water source is configured to introduce water to an SMR tube that has a temperature above the first predetermined value, such that the temperature of the SMR tube is reduced.

Abstract translation: 提供了用于降低蒸汽甲烷重整器（SMR）管温度的装置。 该装置可以包括SMR炉，与SMR炉连通的监测系统和与SMR炉流体连通的水源。 SMR炉包括设置在SMR炉内的多个SMR管。 监视系统被配置为监测至少多个SMR管的温度并将温度与第一预定值进行比较，并且水源被配置为将水引入具有高于第一预定值的温度的SMR管， 使得SMR管的温度降低。

公开(公告)号：US09321684B2

公开(公告)日：2016-04-26

申请号：US13882284

申请日：2011-10-27

Applicant: Francois Hue ,  Michel Pasquier ,  Martine Pasquier ,  Philippe Lac

Inventor： Francois Hue ,  Michel Pasquier ,  Philippe Lac

IPC: B01J7/00 ,  C04B7/60 ,  C04B7/24 ,  C04B7/28 ,  C04B7/36 ,  C04B7/44 ,  C10J3/84 ,  C10K1/00 ,  F27B7/20 ,  F23G5/027 ,  C10J3/18

CPC classification number: C04B7/60 ,  B01D2257/2025 ,  B01D2258/0233 ,  C04B7/24 ,  C04B7/28 ,  C04B7/364 ,  C04B7/4446 ,  C10J3/18 ,  C10J3/84 ,  C10J2300/0946 ,  C10J2300/1238 ,  C10J2300/16 ,  C10J2300/1634 ,  C10K1/003 ,  C10K1/004 ,  F23G5/027 ,  F27B7/2025 ,  Y02P40/145

Abstract: A cement clinker manufacturing plant that includes a plant for producing purified syngas, obtained from solid waste, and process for transferring ash recovered from the ash pan of the gasifier to at least one inlet of the feedstock conversion device, which the plant includes, and/or of the furnace for the purpose of incorporating said ash into the feedstock; and a process for conveying the purified syngas to the main tuyere of the furnace and/or to at least one inlet of the feedstock conversion device.

Abstract translation: 一种水泥熟料制造工厂，其包括用于生产从固体废物获得的纯化合成气的设备，以及用于将从气化器的灰盘回收的灰分转移到所述设备包括的原料转化装置的至少一个入口的工艺和/ 或炉子，用于将所述灰分并入原料中; 以及将纯化的合成气输送到炉子的主风口和/或原料转化装置的至少一个入口的方法。

公开(公告)号：US09315746B2

公开(公告)日：2016-04-19

申请号：US13884108

申请日：2011-11-07

Applicant: Yasuharu Matsushita

Inventor： Yasuharu Matsushita

IPC: B01J7/00 ,  C10J3/82 ,  C10J3/26 ,  C10J3/72 ,  C10J3/80 ,  C10K3/00 ,  F23G5/027 ,  F23G5/46 ,  F23G7/10 ,  C01B3/36 ,  F28D20/00 ,  F28D1/053 ,  F28D21/00

CPC classification number: B01J19/24 ,  B01J2219/00103 ,  B01J2219/24 ,  C01B3/32 ,  C01B3/36 ,  C01B2203/025 ,  C01B2203/0255 ,  C01B2203/06 ,  C01B2203/0833 ,  C01B2203/0894 ,  C10J3/26 ,  C10J3/723 ,  C10J3/80 ,  C10J3/82 ,  C10J2200/09 ,  C10J2300/0916 ,  C10J2300/1671 ,  C10J2300/1693 ,  C10J2300/1869 ,  C10J2300/1884 ,  C10J2300/1892 ,  C10K3/005 ,  F23G5/0276 ,  F23G5/46 ,  F23G7/10 ,  F23G2201/40 ,  F23G2206/203 ,  F28D1/05316 ,  F28D20/0056 ,  F28D2021/0075 ,  Y02E20/12 ,  Y02E60/142

Abstract: A gasification furnace for gasifying a biomass resource in a manner producing a low quantity of tar. The gasification furnace (10) is provided with a punching plate (11) partitioning the furnace interior into upper and lower spaces; a biomass resource supply port (10a) for supplying the biomass resource over the punching plate (11); a first oxidizer supply port (10c) and a second oxidizer supply port (10d) for supplying an oxidizer into the furnace; a first oxidizer supply path supplying the oxidizer from the first oxidizer supply port (10c) from above towards below the punching plate (11); a second oxidizer supply path distributing and supplying to a plurality of locations within a predetermined area in the vicinity of the punching plate (11) from the second oxidizer supply port (10d); and a dry distillation gas output (10b) for discharging dry distillation gas generated by the pyrolysis and partial oxidation of the biomass resource on the punching plate (11) to the outside.

Abstract translation: 一种气化炉，以生产少量焦油的方式气化生物质资源。 气化炉（10）设置有将炉内部分隔成上部和下部空间的冲压板（11） 生物质资源供应口（10a），用于在冲孔板（11）上提供生物量资源; 第一氧化剂供给口（10c）和用于将氧化剂供给到炉中的第二氧化剂供给口（10d） 从所述第一氧化剂供给口（10c）向所述冲压板（11）的下方供给所述氧化剂的第一氧化剂供给路径。 第二氧化剂供给路径，从所述第二氧化剂供给口（10d）向所述冲压板（11）附近的规定区域内的多个位置分配供给。 以及用于将通过冲压板（11）上的生物量资源的热解和部分氧化产生的干馏气体排出到外部的干馏气体输出（10b）。

公开(公告)号：US09315735B2

公开(公告)日：2016-04-19

申请号：US14216692

申请日：2014-03-17

Applicant: Randall Cole ,  Seth Murphy ,  Ronald Bruer ,  Edmund Kaminski ,  Peter Sach

Inventor： Randall Cole ,  Seth Murphy ,  Ronald Bruer ,  Edmund Kaminski ,  Peter Sach

IPC: C10B49/14 ,  C10J3/57 ,  B01J7/00 ,  C10G2/00 ,  C10L3/08 ,  C01B3/34

CPC classification number: C01B3/32 ,  C01B3/342 ,  C01B3/348 ,  C01B2203/04 ,  C01B2203/0405 ,  C01B2203/0415 ,  C01B2203/0465 ,  C01B2203/061 ,  C01B2203/062 ,  C01B2203/0833 ,  C01B2203/0861 ,  C01B2203/142 ,  C07C29/1518 ,  C10G2/30 ,  C10G2/32 ,  C10L1/04 ,  C10L3/08 ,  C10L2290/04 ,  C10L2290/26 ,  C10L2290/38 ,  C10L2290/42 ,  C10L2290/547 ,  C12P5/023 ,  Y02E20/18 ,  Y02E50/13 ,  Y02E50/18 ,  Y02E50/343 ,  Y02P30/10

Abstract: A system and method for converting waste and secondary materials into synthesis gas (syngas) through the use of a molten metal bath gasifier for the initial breakdown of waste feeds and an A/C plasma reactor for complete dissociation of waste feeds into syngas, and an anaerobic digester. The system includes a heat recovery and steam power generation process for the production of electricity. The system produces a net output of electricity above plant load sufficient for the co-production of renewable Hydrogen and Oxygen. The process does not require the use of fossil fuels or fossil feedstocks during normal operations, and it eliminates combustion produced stack emissions or landfill residuals.

Abstract translation: 一种通过使用熔融金属浴气化器将废料和二次物质转化成合成气（合成气）用于废料初始分解和用于将废料完全分解成合成气的A / C等离子体反应器的系统和方法，以及 厌氧消化器 该系统包括用于生产电力的热回收和蒸汽发电过程。 该系统产生的电力净值高于工厂负荷，足以共同生产可再生氢气和氧气。 该过程在正常运行期间不需要使用化石燃料或化石原料，并且消除燃烧产生的烟囱排放物或垃圾填埋残余物。

公开(公告)号：US09314762B2

公开(公告)日：2016-04-19

申请号：US13869192

申请日：2013-04-24

Applicant: Institute of Nuclear Energy Research, Atomic Energy Council, Executive Yuan, R.O.C.

Inventor： Yu Chao ,  Chin-Lee Chiu ,  Ching-Kuei Chen ,  Wen-Tang Hong

IPC: B01J7/00 ,  B01J12/00 ,  B01J19/00 ,  B01J4/00 ,  C01B3/32

CPC classification number: B01J12/005 ,  B01J4/008 ,  B01J12/00 ,  B01J19/0026 ,  B01J2219/00159 ,  C01B3/32 ,  Y02P20/129

Abstract: A novel reformer is provided. A gas fuel is guided from a fuel channel. Air and water are guided from a liquid/gas channel. They are mixed together in a mixing space. On mixing them, the temperature of the mixing space is between 150° C. and 300° C. Thus, the reactants are preheated and fully mixed; and a proper temperature is reached to avoid local over-heating and to prevent carbon deposited.

Abstract translation: 提供了一种新的改良剂。 气体燃料从燃料通道引导。 空气和水从液体/气体通道引导。 它们在混合空间中混合在一起。 在混合它们时，混合空间的温度在150℃和300℃之间。因此，将反应物预热并充分混合; 并达到适当的温度以避免局部过热并防止碳沉积。

公开(公告)号：US09309473B2

公开(公告)日：2016-04-12

申请号：US14215767

申请日：2014-03-17

Applicant: McAlister Technologies, LLC

Inventor： Roy Edward McAlister

IPC: C10J1/26 ,  B01J7/00 ,  B63B35/44 ,  C01B3/34 ,  E21B43/01 ,  E21B43/24 ,  F24J2/04 ,  F24J2/07 ,  F24J3/06 ,  F24J3/08 ,  F28D15/02

CPC classification number: C10J1/26 ,  B01J7/00 ,  B63B35/4413 ,  C01B3/24 ,  C01B3/32 ,  C01B3/34 ,  C01B2203/0205 ,  C01B2203/025 ,  C01B2203/0266 ,  C01B2203/061 ,  C01B2203/1217 ,  C01B2203/1241 ,  E21B43/0122 ,  E21B43/24 ,  E21B2043/0115 ,  F02M21/0206 ,  F02M21/0215 ,  F02M21/0227 ,  F02M21/0254 ,  F02M21/0266 ,  F02M21/0287 ,  F02M27/02 ,  F24S10/17 ,  F24S20/20 ,  F24T10/20 ,  F24V50/00 ,  F28D15/02 ,  Y02E10/14 ,  Y02E10/41 ,  Y02E10/44 ,  Y02T10/32

Abstract: Systems and methods for extracting and processing gases from submerged sources are disclosed. A system for removing and processing a gas from a submerged area in accordance with a particular embodiment includes a membrane or other open-bottom structure having a port and being disposed over at least a portion of the submerged area so as to at least partially enclose a volume of the gas. The system can further include a chemical reactor coupled to the open-bottom structure to receive the gas, and positioned to conduct a non-combustion reaction to dissociate a constituent from a donor substance of the gas.

Abstract translation: 公开了用于从浸没源提取和处理气体的系统和方法。 根据特定实施例的用于从浸没区域去除和处理气体的系统包括具有端口并设置在浸没区域的至少一部分上的膜或其它开口底部结构，以至少部分地包围 气体体积。 该系统还可以包括耦合到开口底部结构以接收气体的化学反应器，并且定位成进行非燃烧反应以使组分与气体的供体物质分离。

公开(公告)号：US09303221B2

公开(公告)日：2016-04-05

申请号：US14158305

申请日：2014-01-17

Applicant: General Electric Company

Inventor： Kenneth M. Sprouse ,  Shahram Farhangi ,  Robert M. Saxelby ,  David R. Matthews

IPC: B01J7/00 ,  C10J3/72 ,  C10J3/50 ,  C10K1/16 ,  F23L7/00 ,  F23D1/00 ,  B01F5/02

CPC classification number: C10J3/72 ,  B01F5/0262 ,  C10J3/506 ,  C10J2200/152 ,  C10J2300/165 ,  C10J2300/1653 ,  C10J2300/1675 ,  C10J2300/1678 ,  C10K1/165 ,  F23C2201/20 ,  F23D1/005 ,  F23D2201/10 ,  F23D2213/00 ,  F23D2214/00 ,  F23D2900/00006 ,  F23L7/005 ,  F23L2900/07002 ,  F23L2900/07005 ,  Y02E20/16 ,  Y02E20/18 ,  Y02E20/344 ,  Y10T29/49826 ,  Y10T29/53

Abstract: A method of assembling an injection device for use in a reactor injector feed assembly includes extending the injection device at least partially into a cavity. The injection device includes a plurality of substantially concentric conduits coupled to a modular tip that includes a plurality of cooling channels and a plurality of substantially annular nozzles defined therein. The method also includes coupling at least one coolant distribution device in flow communication with the plurality of cooling channels to facilitate removing heat from an outer surface of the injection device.

Abstract translation: 一种组装用于反应堆注射器进料组件的注射装置的方法包括至少部分地将注射装置延伸到腔中。 注射装置包括耦合到模块化末端的多个基本上同心的导管，其包括多个冷却通道和限定在其中的多个基本上环形的喷嘴。 该方法还包括联接至少一个与多个冷却通道流体连通的冷却剂分配装置，以便于从注射装置的外表面移除热量。

公开(公告)号：US09291394B2

公开(公告)日：2016-03-22

申请号：US13996258

申请日：2011-12-19

Applicant: Didier Lesueur

Inventor： Didier Lesueur

IPC: B01J7/00 ,  F27B14/08 ,  F23G5/027 ,  F23G5/20 ,  F27B14/12 ,  F27B19/04 ,  F27B14/02 ,  F27B19/02

CPC classification number: F27B14/0806 ,  F23G5/0273 ,  F23G5/20 ,  F23G2209/281 ,  F23G2900/50801 ,  F27B14/02 ,  F27B14/08 ,  F27B14/12 ,  F27B19/02 ,  F27B19/04

Abstract: A heating module for heating solid matter, such as balls, to a determined temperature. The module includes a heating pot including a crucible for receiving the matter to be heated, and a burner for heating the crucible and the matter to be heated; and a cover that is mounted in removable manner on the heating pot so as to close the crucible.

Abstract translation: 一种用于将固体物质如球加热至确定温度的加热模块。 该模块包括加热罐，该加热罐包括用于接收被加热物的坩埚和用于加热坩埚和被加热物的燃烧器; 以及以可移动的方式安装在加热罐上以封闭坩埚的盖。

公开(公告)号：US09243197B2

公开(公告)日：2016-01-26

申请号：US13871911

申请日：2013-04-26

Applicant: ENERSOL POWER LLC.

Inventor： Kenneth Hladun ,  Jayaraman Ramamurthi ,  Mark Edward Vetter ,  Yuji Kado

IPC: B01J7/00 ,  C10J3/72 ,  C10J3/00 ,  C10J3/48 ,  C10J3/84 ,  C10K3/00

CPC classification number: C10J3/721 ,  C10J3/00 ,  C10J3/487 ,  C10J3/84 ,  C10J2300/0916 ,  C10J2300/1238 ,  C10J2300/1618 ,  C10K3/003 ,  Y02P20/145

Abstract: A system for producing superior quality synthesis gas (“syngas”) consisting of a series of chambers in which the gasification stages of reaction, homogenization and activation occur. The first stage reaction stage agitates and combines the reactants, consisting primarily of organic matter, oxidizer and steam, to initiate gasification of the organic and volatile fraction and to transport the inorganic residue to continuous removal. In the homogenization chamber, turbulence is induced by injecting gaseous species. The gas mixture emerging from the homogenization chamber is accelerated via a third stage communicating duct and is introduced tangentially into the fourth stage activation chamber inducing a cyclonic motion wherein a high intensity radiant heat source is introduced along the central axis of the gas vortex. The syngas and remaining particulate materials are constrained to exit the activation stage through discrete portals which are oriented to further separate the syngas from the remaining entrained particulates.

Abstract translation: 一种用于生产优质合成气（“合成气”）的系统，其由发生反应，均化和活化的气化阶段的一系列室组成。 第一阶段反应阶段搅动并组合主要由有机物，氧化剂和蒸汽组成的反应物，以引发有机和挥发性部分的气化，并将无机残余物输送到连续除去。 在均化室中，通过注入气态物质诱导湍流。 从均质室出来的气体混合物通过第三级连通管道被加速，并被切向地引入到第四级激活室中，引起气旋运动，其中沿气体涡流的中心轴引入高强度辐射热源。 合成气和剩余的颗粒材料被限制为通过分离的入口离开活化阶段，这些入口被定向以进一步将合成气与剩余的夹带的颗粒分离。

公开(公告)号：US09193923B2

公开(公告)日：2015-11-24

申请号：US13386934

申请日：2010-06-29

Applicant: Thomas Fleischer ,  Frank Hannemann ,  Christian Reuther ,  Manfred Schingnitz ,  Ralph Schumann

Inventor： Thomas Fleischer ,  Frank Hannemann ,  Christian Reuther ,  Manfred Schingnitz ,  Ralph Schumann

IPC: B01J7/00 ,  C10J3/52 ,  C10J3/48 ,  C10J3/76 ,  C10J3/78 ,  C10J3/82 ,  C10J3/84 ,  C10K1/08 ,  C10K1/10

CPC classification number: C10J3/526 ,  C10J3/485 ,  C10J3/76 ,  C10J3/78 ,  C10J3/82 ,  C10J3/84 ,  C10J2200/09 ,  C10J2300/1884 ,  C10J2300/1892 ,  C10K1/08 ,  C10K1/10 ,  C10K1/101 ,  Y02E20/16 ,  Y02E20/18 ,  Y02P20/129

Abstract: An entrained flow gasifier designed as a component for an Integrated Gasification Combined Cycle plant of optimized efficiency is provided. The raw gas initially flows through a waste heat unit designed as a radiation cooler and subsequently flows through a full water quench. This results in a higher ratio of steam in the raw gas, which decreases the medium-pressure steam supply before the water-gas shift and thus improves efficiency in IGCC plants with CO2 separation.

Abstract translation: 提供了一种以优化效率为综合气化联合循环设备的组件设计的夹带式流化气化器。 原始气体最初流经设计为辐射冷却器的废热单元，随后流经全水淬。 这导致原始气体中的蒸汽比例较高，这降低了在水煤气变化之前的中压蒸汽供应，从而提高了具有二氧化碳分离的IGCC设备的效率。