公开(公告)号：US20160152905A1

公开(公告)日：2016-06-02

申请号：US14952060

申请日：2015-11-25

Applicant: Sundrop Fuels, Inc.

Inventor： Renus C. Kelfkens ,  Wayne W. Simmons ,  Douglas S. Jack ,  Jerrod Wayne Hohman ,  Sidney P. White

IPC: C10J3/46 ,  C10J3/50 ,  C01B3/38 ,  C10K3/00 ,  C10G2/00 ,  C10L1/04 ,  C10J3/48 ,  C10J3/84

CPC classification number: C10J3/466 ,  C01B3/38 ,  C01B2203/0233 ,  C01B2203/062 ,  C01B2203/1241 ,  C10G2/32 ,  C10G2/34 ,  C10G3/00 ,  C10G45/00 ,  C10G45/44 ,  C10G2300/1011 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10J3/485 ,  C10J3/506 ,  C10J3/84 ,  C10J2300/0916 ,  C10J2300/0976 ,  C10J2300/1659 ,  C10J2300/1807 ,  C10J2300/1853 ,  C10K1/08 ,  C10K1/32 ,  C10K3/008 ,  C10K3/023 ,  C10L1/04 ,  C10L2200/0492 ,  C10L2270/023 ,  C10L2270/026 ,  C10L2270/04 ,  C10L2290/04 ,  C10L2290/06 ,  C10L2290/10 ,  C10L2290/42 ,  C10L2290/541 ,  C10L2290/542 ,  C10L2290/543 ,  C10L2290/548 ,  Y02E50/32 ,  Y02P20/145 ,  Y02P20/582 ,  Y02P30/20

Abstract: An integrated plant to generate chemical grade syngas from a steam biomass reforming in a multiple stage bio reforming reactor for use with either a high temperature or low temperature Fischer-Tropsch synthesis process to produce fuel from biomass is discussed. The first stage has a reactor to cause a chemical devolatilization of a biomass feedstock from the biomass feedstock supply lines into its constituent gases of CO, H2, CO2, CH4, tars, chars, and other components into a raw syngas mixture. A second stage performs further reforming of the raw syngas from the first stage into the chemical grade syngas by further applying heat and pressure to chemically crack at least the tars, reform the CH4, or a combination of both, into their corresponding syngas molecules. The second stage feeds the chemical grade syngas derived from the biomass feedstock to the downstream Fischer-Tropsch train to produce the fuel from the biomass. One or more recycle loops supply tail gas or FT product back into the plant.

Abstract translation: 讨论了一种用于在多级生物重整反应器中从蒸汽生物质重整产生化学级合成气的综合工厂，用于与高温或低温费 - 托合成方法一起使用以从生物质产生燃料。 第一阶段具有反应器，以使生物质原料从生物质原料供应管线进入其CO，H 2，CO 2，CH 4，焦油，焦炭和其它组分的组成气体的化学脱挥发分成原始合成气混合物。 第二阶段通过进一步施加热和压力来将原料合成气从第一阶段进一步重整成化学级合成气，至少化学裂化焦油，将CH 4或两者的组合重整成相应的合成气分子。 第二阶段将来自生物质原料的化学级合成气进料到下游费 - 托列车，以从生物质产生燃料。 一个或多个回收循环将尾气或FT产物回送到工厂。

公开(公告)号：US20160122669A1

公开(公告)日：2016-05-05

申请号：US14533838

申请日：2014-11-05

Applicant: General Electric Company

Inventor： Hidayathullah Shaik Mohammad ,  Sethuraman Balasubramaniyan ,  John Saunders Stevenson ,  Thomas Frederick Leininger

IPC: C10J3/00 ,  C10J3/72 ,  C10J3/20

CPC classification number: C10J3/485 ,  C10J3/721 ,  C10J3/86 ,  C10J2300/092 ,  C10J2300/093 ,  C10J2300/0943 ,  C10J2300/0946 ,  Y02E20/18

Abstract: A system includes an integrated reactor-syngas cooler that may gasify a feedstock. The integrated reactor-syngas cooler includes a reaction zone that may receive a first syngas and the feedstock, and that may gasify the feedstock to generate a second syngas. The second syngas has a composition different from the first syngas. The system also includes one or more feed injectors disposed in the integrated reactor-syngas cooler and that may supply the feedstock to the reaction zone and a cooling zone disposed downstream of the reaction zone and including one or more cooling tubes. The cooling zone may receive and cool the second syngas.

Abstract translation: 系统包括可将原料气化的集成反应器 - 合成气冷却器。 集成的反应器 - 合成气冷却器包括可以接收第一合成气和原料的反应区，并且可以将原料气化以产生第二合成气。 第二合成气具有不同于第一合成气的组成。 该系统还包括设置在集成反应器 - 合成气冷却器中的一个或多个进料喷射器，并且可以将原料供应到反应区和设置在反应区下游并包括一个或多个冷却管的冷却区。 冷却区可以接收和冷却第二合成气。

公开(公告)号：US09309464B2

公开(公告)日：2016-04-12

申请号：US13878884

申请日：2011-10-10

Applicant: Rolf Ljunggren

Inventor： Rolf Ljunggren

IPC: C10J3/00 ,  C10B21/00 ,  C10B47/18 ,  C10J3/48

CPC classification number: C10B21/00 ,  C10B47/18 ,  C10J3/485 ,  C10J2300/093 ,  C10J2300/0969 ,  C10J2300/0976 ,  C10J2300/1207 ,  C10J2300/1269 ,  C10J2300/1625 ,  C10J2300/1884 ,  C10J2300/1892 ,  Y02P20/129

Abstract: Method and equipment for producing coke (PC) during indirectly heated gasification, in which coal particles are supplied to a gasification reactor (1) and process gas (P) supplied during the gasification is reduced in it to synthesis gas (S), whereby the synthesis gas (S) is removed from the gasification reactor (1). The method is distinguished in that at the same time a gasification takes place, a coking of coal takes place in an inner reactor (4) arranged inside the gasification reactor (1), that the inner reactor (4) is indirectly heated, that coke (PC) and combustible gases are produced in the inner reactor (4) during the coking, and that the combustible gases are used for the indirect heating in the gasification in the gasification reactor (1).

Abstract translation: 在气化过程中将煤粒子供给到气化反应器（1）和处理气体（P）的间接加热气化过程中生产焦炭（PC）的方法和设备减少到合成气体（S），由此 从气化反应器（1）除去合成气（S）。 该方法的特征在于，同时发生气化，煤焦化在布置在气化反应器（1）内的内反应器（4）中发生，内反应器（4）被间接加热，焦炭 （PC）和可燃气体在焦化期间在内反应器（4）中产生，并且可燃气体用于气化反应器（1）中的气化中的间接加热。

公开(公告)号：US20160002547A1

公开(公告)日：2016-01-07

申请号：US14851633

申请日：2015-09-11

Applicant: RES USA, LLC

Inventor： Weibin Jiang ,  Bruce E. McComish ,  Bryan C. Borum ,  Benjamin H. Carryer ,  Mark K. Robertson ,  Eric R. Elrod ,  Sim Weeks ,  Harold A. Wright

IPC: C10J3/72 ,  C10G2/00 ,  C10K1/00 ,  C10K1/22 ,  C10J3/48 ,  C10K3/00

CPC classification number: C10J3/721 ,  B01J8/18 ,  C01B2203/0244 ,  C01B2203/025 ,  C01B2203/0283 ,  C01B2203/0405 ,  C01B2203/0415 ,  C01B2203/043 ,  C01B2203/0475 ,  C01B2203/048 ,  C01B2203/0485 ,  C01B2203/062 ,  C01B2203/0877 ,  C01B2203/146 ,  C10G2/00 ,  C10G2/30 ,  C10G2/34 ,  C10G49/007 ,  C10J3/48 ,  C10J3/482 ,  C10J3/485 ,  C10J3/50 ,  C10J2200/09 ,  C10J2300/0909 ,  C10J2300/0916 ,  C10J2300/093 ,  C10J2300/0943 ,  C10J2300/0969 ,  C10J2300/0976 ,  C10J2300/0993 ,  C10J2300/1606 ,  C10J2300/1643 ,  C10J2300/1659 ,  C10J2300/1671 ,  C10J2300/1807 ,  C10J2300/1815 ,  C10J2300/1823 ,  C10K1/005 ,  C10K1/22 ,  C10K1/32 ,  C10K3/00 ,  C10K3/04

Abstract: A system for the production of synthesis gas, including a gasification apparatus configured to convert at least a portion of a gasifier feed material introduced thereto into a gasification product gas comprising synthesis gas having a molar ratio of hydrogen to carbon monoxide; at least one additional apparatus selected from the group consisting of feed preparation apparatus located upstream of the gasification apparatus, synthesis gas conditioning apparatus, and synthesis gas utilization apparatus; and at least one line fluidly connecting the at least one additional apparatus or an outlet of the gasification apparatus with the at least one vessel of the gasification apparatus, whereby a gas from the at least one additional apparatus or exiting the gasification apparatus may provide at least one non-steam component of a fluidization gas. A method of utilizing the system is also provided.

Abstract translation: 一种用于生产合成气的系统，包括气化装置，其被配置为将引入到其中的气化器进料的至少一部分转化成包含氢与一氧化碳摩尔比的合成气的气化产物气体; 至少一种选自由气化装置上游的进料制备装置，合成气调节装置和合成气利用装置组成的组的附加装置; 以及将所述气化装置的所述至少一个附加装置或出口与所述气化装置的所述至少一个容器流体连接的至少一个管线，由此来自所述至少一个附加装置或离开所述气化装置的气体可以至少提供 流化气体的一种非蒸汽组分。 还提供了利用该系统的方法。

公开(公告)号：US09221681B2

公开(公告)日：2015-12-29

申请号：US14219987

申请日：2014-03-19

Applicant: Enventix, Inc.

Inventor： Abdelmonem Hussein Alyaser

IPC: C07C27/00 ,  C01B3/02 ,  C01B3/32 ,  C01B3/36 ,  F01K23/06 ,  C10J3/48 ,  C10J3/72 ,  C10J3/86 ,  C10K1/00 ,  C10K1/34

CPC classification number: C01B3/02 ,  C01B3/32 ,  C01B3/36 ,  C01B2203/0255 ,  C01B2203/0465 ,  C01B2203/0475 ,  C01B2203/0485 ,  C01B2203/06 ,  C01B2203/061 ,  C01B2203/0894 ,  C01B2203/1211 ,  C01B2203/86 ,  C07C27/00 ,  C10J3/485 ,  C10J3/721 ,  C10J3/86 ,  C10J2300/0916 ,  C10J2300/093 ,  C10J2300/0969 ,  C10J2300/0973 ,  C10J2300/0976 ,  C10J2300/1246 ,  C10J2300/1621 ,  C10J2300/1628 ,  C10J2300/1653 ,  C10J2300/1665 ,  C10J2300/1696 ,  C10J2300/1853 ,  C10J2300/1876 ,  C10J2300/1884 ,  C10J2300/1892 ,  C10K1/002 ,  C10K1/003 ,  C10K1/34 ,  F01K23/067 ,  Y02E20/16 ,  Y02E20/18 ,  Y02E20/185 ,  Y02E50/18 ,  Y02E50/32 ,  Y02P20/145 ,  Y02P30/30

Abstract: A system and method for providing an integrated indirectly fired reactor and steam generator are disclosed. According to one embodiment, the reactor comprises an indirect heating zone heating water and generating steam, a mixing zone mixing feedstock and the steam and providing a mixture of the feedstock and the steam, and a reaction zone comprising a first reactor and a second reactor. The first reactor converts the mixture to a first syngas at a first temperature. The second reactor converts the first syngas to a second syngas at a second temperature, the second temperature being higher than the first temperature.

Abstract translation: 公开了一种用于提供集成的间接发射的反应器和蒸汽发生器的系统和方法。 根据一个实施方案，反应器包括加热水和产生蒸汽的间接加热区，混合原料和蒸汽的混合区，并提供原料和蒸汽的混合物，以及包含第一反应器和第二反应器的反应区。 第一反应器将混合物在第一温度下转化为第一合成气。 第二反应器在第二温度下将第一合成气转化为第二合成气，第二温度高于第一温度。

公开(公告)号：US20150275112A1

公开(公告)日：2015-10-01

申请号：US14439328

申请日：2013-10-30

Applicant: IFP ENERGIES NOUVELLES ,  AXENS ,  BIONEXT ,  COMMISSARIAT A L'ENERGIE ATOMIQUE ET AUX ENERGIES ALTERNATIVES ,  SOFIPROTEOL ,  THYSSENKRUPP UHDE GMBH ,  TOTAL RAFFINAGE CHIMIE

Inventor： Guillaume Boissonnet ,  Michael Hecquet ,  Priscilla Avenier ,  Laurent Bournay ,  David Chiche ,  Jean-Philippe Heraud ,  Anne Claire Lucquin ,  Norbert Ullrich ,  Stéphane Fedou ,  Julien Rousseau ,  Raphael Lemaire ,  Jean-Christophe Viguie

IPC: C10K3/04 ,  C10G45/00 ,  C10G47/00 ,  C10J3/46 ,  C10K3/06 ,  C10K1/00 ,  C10K1/10 ,  C10K1/34 ,  C10K1/20 ,  C10G2/00 ,  C10J3/48

CPC classification number: C10K3/04 ,  B01J20/06 ,  B01J20/18 ,  B01J20/20 ,  B01J2220/603 ,  C10G2/30 ,  C10G2/32 ,  C10G45/00 ,  C10G47/00 ,  C10G2300/1011 ,  C10J3/00 ,  C10J3/466 ,  C10J3/485 ,  C10J2200/09 ,  C10J2300/0906 ,  C10J2300/0909 ,  C10J2300/0916 ,  C10J2300/0959 ,  C10J2300/1659 ,  C10J2300/1846 ,  C10K1/004 ,  C10K1/005 ,  C10K1/006 ,  C10K1/007 ,  C10K1/101 ,  C10K1/20 ,  C10K1/34 ,  C10K3/06 ,  C10L9/083 ,  Y02E50/15 ,  Y02E50/32 ,  Y02P20/125 ,  Y02P20/145 ,  Y02P20/52 ,  Y02P30/10 ,  Y02P30/20

Abstract: The present invention concerns an integrated process for the production of liquid hydrocarbons starting from a feed containing at least one fraction of biomass and optionally at least one fraction of another feed, said process comprising at least one pre-treatment step, a gasification step, a step for conditioning synthesis gas, a water scrubbing step, a step for eliminating acid gases, a final purification step, and a catalytic Fischer-Tropsch synthesis reaction step.

Abstract translation: 本发明涉及从含有至少一部分生物质和任选的至少一个其它进料部分的进料开始生产液体烃的综合方法，所述方法包括至少一个预处理步骤，气化步骤， 用于调节合成气的步骤，水洗步骤，消除酸性气体的步骤，最终纯化步骤和催化费 - 托合成反应步骤。

公开(公告)号：US09127220B2

公开(公告)日：2015-09-08

申请号：US13111836

申请日：2011-05-19

Applicant: Randy Blevins ,  Joshua B. Pearson ,  Harold A. Wright

Inventor： Randy Blevins ,  Joshua B. Pearson ,  Harold A. Wright

IPC: B01J7/00 ,  C10J3/30 ,  B01J8/06 ,  B01J19/24 ,  C10J3/48 ,  C10J3/80 ,  F23G5/033 ,  F23G5/04 ,  F23G5/44

CPC classification number: C10J3/466 ,  B01J8/067 ,  B01J19/2415 ,  B01J19/242 ,  B01J19/2425 ,  B01J19/243 ,  B01J2208/00309 ,  B01J2208/00504 ,  B01J2219/00006 ,  B01J2219/00157 ,  B01J2219/00159 ,  B01J2219/24 ,  C01B3/02 ,  C01B3/346 ,  C01B2203/0216 ,  C01B2203/0811 ,  C01B2203/1241 ,  C10G2/30 ,  C10G2/34 ,  C10J3/30 ,  C10J3/485 ,  C10J3/80 ,  C10J2200/09 ,  C10J2300/0906 ,  C10J2300/0909 ,  C10J2300/0916 ,  C10J2300/0976 ,  C10J2300/1223 ,  C10J2300/1246 ,  C10J2300/1659 ,  C10J2300/1687 ,  C10J2300/1853 ,  F23G5/033 ,  F23G5/04 ,  F23G5/444 ,  Y02E50/32 ,  Y02P20/145

Abstract: A system for the production of synthesis gas, the system including a mixing apparatus configured for combining steam with at least one carbonaceous material to produce a reformer feedstock; and a reformer comprising a cylindrical vessel containing a plurality of coiled tubes, wherein each of the plurality of coiled tubes has a vertical height in the range of from about 40 feet 12.2 m) to about 100 feet (30.5 m) and a coil length that is at least four times the vertical height; at least one burner configured to combust a fuel and provide heat to maintain the reformer at a reformer temperature; at least one outlet for reformer product comprising synthesis gas; and at least one outlet for flue gas produced via combustion of fuel in the burners. A suitable mixing apparatus is also provided.

Abstract translation: 一种用于生产合成气的系统，该系统包括配置用于将蒸汽与至少一种碳质材料组合以产生重整器原料的混合装置; 以及重整器，其包括容纳多个螺旋管的圆柱形容器，其中所述多个螺旋管中的每一个具有在约40英尺12.2m至约100英尺（30.5m）的范围内的垂直高度和线圈长度， 至少是垂直高度的四倍; 至少一个燃烧器，其构造成燃烧燃料并提供热量以将所述重整器维持在重整器温度; 至少一个包含合成气的重整产物出口; 以及至少一个通过燃烧器中的燃料燃烧产生的用于烟道气的出口。 还提供了合适的混合装置。

公开(公告)号：US20150247099A1

公开(公告)日：2015-09-03

申请号：US14429853

申请日：2013-01-24

Applicant: PRATT & WHITNEY ROCKETDYNE, INC.

Inventor： Steven P. Fusselman

IPC: C10J3/84 ,  C10K1/00 ,  C10K1/02

CPC classification number: C10J3/845 ,  C10J3/485 ,  C10J3/52 ,  C10J2200/09 ,  C10J2300/0959 ,  C10J2300/0976 ,  C10J2300/1625 ,  C10J2300/169 ,  C10J2300/1807 ,  C10K1/003 ,  C10K1/007 ,  C10K1/02 ,  C10K1/024 ,  C10K1/122

Abstract: A gasification system includes a scrubber in communication with a particulate removal subsystem and a quench sub-system

Abstract translation: 气化系统包括与微粒去除子系统和骤冷子系统连通的洗涤器

公开(公告)号：US09115322B2

公开(公告)日：2015-08-25

申请号：US14000917

申请日：2012-02-22

Applicant: Ibrahim Kar ,  Manfred Heinrich Schmitz-Goeb

Inventor： Ibrahim Kar ,  Manfred Heinrich Schmitz-Goeb

IPC: C10J3/74 ,  C10J3/76 ,  C10J3/72 ,  C10J3/48 ,  C10J3/78

CPC classification number: C10J3/723 ,  C10J3/485 ,  C10J3/76 ,  C10J3/78 ,  C10J2200/09

Abstract: A gasification reactor comprising a pressure vessel encasing a gasifier. Strain gauges are provided in the space between the gasifier tubular wall and the pressure vessel on one or more parts loaded by weight of slag within the gasifier, at the exterior surface of the gasifier tubular wall and/or coolant supply lines. Formation of slag deposits and/or pressure within the gasifier is monitored by measuring strain development in parts exposed to stress induced by weight of the slag deposits or induced by internal pressure, respectively.

Abstract translation: 一种气化反应器，包括封装气化器的压力容器。 在气化器管壁和压力容器之间的空间中，在气化器内的炉渣重量的一个或多个部分，气化器管壁和/或冷却剂供应管的外表面处设置应变计。 通过测量暴露于由渣沉积物的重量或由内部压力引起的应力引起的应力的部分中的应变发展来监测气化器中的渣沉积物和/或压力的形成。

公开(公告)号：US09080768B2

公开(公告)日：2015-07-14

申请号：US13671597

申请日：2012-11-08

Applicant: General Electric Company

Inventor： John Caleb Wilson ,  Jennifer Lucia Ramirez ,  James Scott Kain ,  Shaoping Shi ,  Dinh-Cuong Vuong ,  Edward Pan

IPC: C10J3/00 ,  F23M5/06 ,  F23C5/08 ,  C10J3/48 ,  C10J3/72

CPC classification number: F23M5/06 ,  C10J3/485 ,  C10J3/726 ,  C10J2200/152 ,  C10J2300/1653 ,  F23C5/08 ,  Y02E20/18 ,  Y10T29/49348

Abstract: Gasifier preheater fuel and moderator injection apparatus, systems and methods are provided. A preheater distributor ring is securely mounted within the shell dome of a gasification vessel, for the selective discharge of preheat fuel and oxidizer into the vessel during preheating operations, or for the selective discharge of moderating agents into the vessel during normal gasification operations.

Abstract translation: 提供气化器预热器燃料和调节剂注入装置，系统和方法。 预热器分配器环牢固地安装在气化容器的壳体圆顶内，用于在预热操作期间将预热燃料和氧化剂选择性地排放到容器中，或者用于在正常气化操作期间选择性地将调节剂排放到容器中。