公开(公告)号：US1480152A

公开(公告)日：1924-01-08

申请号：US16204117

申请日：1917-04-14

Applicant: GEN REDUCTION GAS & BY PRODUCT

Inventor： COX ABRAHAM B

IPC: C10J3/06

CPC classification number: C10J3/06

公开(公告)号：US11753596B2

公开(公告)日：2023-09-12

申请号：US16237777

申请日：2019-01-02

Applicant: King Fahd University of Petroleum and Minerals

Inventor： Mohammad Mozahar Hossain ,  Tareq Ali Salem Al-Attas

IPC: C10J3/06 ,  C10J3/20 ,  C01B3/02

CPC classification number: C10J3/06 ,  C01B3/02 ,  C10J3/20 ,  C10J2300/092 ,  C10J2300/0906 ,  C10J2300/0916 ,  C10J2300/0953 ,  C10J2300/0956 ,  C10J2300/0969

Abstract: The invention is directed to a co-gasification process that uses biomass and VGO as a feedstock to produce syngas which includes a mixture of carbon monoxide and hydrogen.

公开(公告)号：US10093874B2

公开(公告)日：2018-10-09

申请号：US14663205

申请日：2015-03-19

Applicant: University of Wyoming

Inventor： Maohong Fan ,  Rodolfo Monterrozo

IPC: C10J3/06 ,  C10J3/46 ,  C10J3/02

Abstract: Embodiments described herein generally relate to iron carbonate utilized as a catalyst in coal gasification processes. An FeCO3 catalyst is active in both pyrolysis and gasification operations, and may increase carbon conversion rate and reduce the activation energy of coal gasification. Methods described herein also include suitable processing conditions for performing coal gasification with the FeCO3 catalyst.

公开(公告)号：US09499753B2

公开(公告)日：2016-11-22

申请号：US14650997

申请日：2013-12-11

Applicant: SK INNOVATION CO., LTD. ,  SK ENERGY CO., LTD.

Inventor： Jong Sung Park ,  Ji Sung Park ,  Cheon Seong Lee ,  Gyoo Tae Kim ,  Jae Wook Shin ,  Yong Jeon Kim

IPC: C01B3/38 ,  C10J3/06 ,  C01B3/16 ,  C10J3/12 ,  C10K3/04 ,  C10J3/20

CPC classification number: C10J3/06 ,  C01B3/16 ,  C01B2203/0288 ,  C01B2203/1023 ,  C01B2203/1047 ,  C01B2203/1076 ,  C10J3/12 ,  C10J3/20 ,  C10J2200/09 ,  C10J2300/0909 ,  C10J2300/0959 ,  C10J2300/0969 ,  C10J2300/1823 ,  C10K3/04 ,  Y02E20/18

Abstract: The present invention relates to a gasification process and system, wherein a dryer integrated with a water-gas-shift catalyst is disposed in front of a gasifier.

Abstract translation: 本发明涉及一种气化方法和系统，其中与气 - 气 - 变换催化剂结合的干燥器设置在气化器前面。

公开(公告)号：US09464243B2

公开(公告)日：2016-10-11

申请号：US14552910

申请日：2014-11-25

Applicant: Lingzeng Kong

Inventor： Lingzeng Kong

IPC: C10J3/42 ,  C10J3/06

CPC classification number: C10J3/42 ,  C10J3/06 ,  C10J2300/0906 ,  C10J2300/0916 ,  C10J2300/093 ,  Y02E20/16 ,  Y02E50/10 ,  Y02E50/30

Abstract: The present disclosure provides methods and devices for preparing the fuel gas used. A device may include a furnace body, a tower type synchronous roller extruding machine with a circular ladder groove mold that is mounted at the upper end of the furnace body. The tower type synchronous roller extruding machine is provided with a bucket, the bucket is in airtight connection with the furnace body, and a first transmission shaft is mounted in the bucket. At least two tower type synchronous rollers are mounted on the first transmission shaft, and the tower type synchronous rollers are symmetrically distributed on both sides of the first transmission shaft.

公开(公告)号：US20160244674A1

公开(公告)日：2016-08-25

申请号：US15032310

申请日：2014-10-29

Applicant: THE CRUCIBLE GROUP PTY LTD

Inventor： Lazer Strezov ,  Steve Osborn ,  Joseph George Herberston

IPC: C10B53/02 ,  C10B49/04 ,  C10B25/24 ,  C10B37/04 ,  C10J3/06 ,  C10B7/10

CPC classification number: C10B53/02 ,  B01J2208/00769 ,  B65G33/00 ,  B65G33/24 ,  B65G33/26 ,  B65G33/30 ,  B65G33/34 ,  C10B7/10 ,  C10B25/24 ,  C10B37/04 ,  C10B47/34 ,  C10B47/44 ,  C10B49/02 ,  C10B49/04 ,  C10J3/06 ,  C10J2300/0916 ,  C10J2300/093 ,  C10J2300/0946 ,  C10J2300/0959 ,  C10J2300/1846 ,  Y02E50/14 ,  Y02P20/145

Abstract: A continuous converter for pyrolysing or otherwise processing biomass or other solid organic feed materials includes a reaction chamber (5) for producing a solid carbon-containing product and a gas product and optionally a liquid water product via pyrolysis or other reaction mechanisms from a solid organic feed material. The chamber has an inlet (41) for supplying a solid organic feed material to the chamber and separate outlets (15, 35) for the solid carbon-containing product and the gas product produced in the reaction chamber. The inlet and the solid carbon-containing product outlet are configured so that the solid materials in the inlet and in the outlet form respective gas seals in the inlet and the outlet.

Abstract translation: 用于热解或以其它方式处理生物质或其它固体有机进料的连续转化器包括用于通过热解或其它反应机理从固体有机物产生固体含碳产物和气体产物以及任选的液体水产物的反应室（5） 饲料 该室具有用于向室提供固体有机进料的入口（41）和用于固体含碳产物的分离出口（15,35）和在反应室中产生的气体产物。 入口和固体含碳产品出口构造成使得入口和出口中的固体材料在入口和出口处形成相应的气体密封。

公开(公告)号：US09376318B2

公开(公告)日：2016-06-28

申请号：US14504295

申请日：2014-10-01

Applicant: The Ohio State University

Inventor： Liang-Shih Fan ,  Fanxing Li

IPC: B01J19/30 ,  C01B3/34 ,  C10J3/12 ,  C10J3/46 ,  C10J3/72 ,  F23C99/00 ,  C01B3/02 ,  C01B3/32 ,  C10J3/02 ,  C10J3/06

CPC classification number: C10J3/725 ,  B01J19/245 ,  B01J2219/19 ,  B01J2219/24 ,  C01B3/02 ,  C01B3/344 ,  C10J3/12 ,  C10J3/463 ,  C10J3/485 ,  C10J2300/0916 ,  C10J2300/093 ,  C10J2300/0943 ,  C10J2300/0959 ,  C10J2300/0969 ,  C10J2300/0976 ,  C10J2300/1671 ,  C10J2300/1807 ,  C10J2300/1869 ,  C10J2300/1884 ,  F23C99/00 ,  F23C2900/99008 ,  Y02E20/16 ,  Y02E20/346 ,  Y02P20/52 ,  Y10T428/2982

Abstract: A system for converting fuel is provided and includes a first reactor comprising a plurality of ceramic composite particles, the ceramic composite particles comprising at least one metal oxide disposed on a support, wherein the first reactor is configured to reduce the at least one metal oxide with a fuel to produce a reduced metal or a reduced metal oxide; a second reactor configured to oxidize at least a portion of the reduced metal or reduced metal oxide from the said first reactor to produce a metal oxide intermediate; a source of air; and a third reactor communicating with said source of air and configured to regenerate the at least one metal oxide from the remaining portion of the solids discharged from the said first reactor and the solids discharged from the said second reactor by oxidizing the metal oxide intermediate.

Abstract translation: 提供了用于转化燃料的系统，并且包括包含多个陶瓷复合颗粒的第一反应器，所述陶瓷复合颗粒包含设置在载体上的至少一种金属氧化物，其中所述第一反应器构造成用至少一种金属氧化物还原所述至少一种金属氧化物 产生还原金属或还原金属氧化物的燃料; 第二反应器，被配置为从所述第一反应器氧化至少一部分还原金属或还原的金属氧化物以产生金属氧化物中间体; 空气来源 以及第三反应器，其与所述空气源连通并且被配置为从所述第一反应器排出的固体的剩余部分和通过氧化金属氧化物中间体从所述第二反应器排出的固体再生至少一种金属氧化物。

公开(公告)号：US20080034660A1

公开(公告)日：2008-02-14

申请号：US10592542

申请日：2005-03-07

Applicant: Martin Keyser ,  Roelof Lodewyk Coetzer ,  Johannes Van Dyk

Inventor： Martin Keyser ,  Roelof Lodewyk Coetzer ,  Johannes Van Dyk

IPC: C10J3/06

CPC classification number: C10J3/06 ,  C10J3/721 ,  C10J2300/0906 ,  C10J2300/093 ,  C10J2300/0959 ,  C10J2300/1846

Abstract: A process for gasifying a carbonaceous particulate feedstock includes dividing the carbonaceous particulate feedstock into at least two feedstock fractions, each feedstock fraction including particulate material within a predetermined particle size range so that there are at least a smaller particle size feedstock and a larger particle size feedstock. The smaller particle size feedstock is fed to at least one gasifier and the larger particle size feedstock is fed to at least one other gasifier.

Abstract translation: 用于气化碳质颗粒原料的方法包括将碳质颗粒原料分成至少两个原料馏分，每个原料馏分包括预定粒度范围内的颗粒材料，使得至少具有较小的颗粒尺寸的原料和较大的颗粒尺寸原料 。 将较小颗粒尺寸的原料进料至至少一个气化器，并将较大颗粒尺寸的原料进料至至少一个其它气化器。

公开(公告)号：US20050279711A1

公开(公告)日：2005-12-22

申请号：US10963408

申请日：2004-10-12

Applicant: Keith Goettert ,  Richard Kleinke ,  Paul Finestone

Inventor： Keith Goettert ,  Richard Kleinke ,  Paul Finestone

IPC: B01D61/02 ,  B01D61/58 ,  C02F1/00 ,  C02F1/02 ,  C02F1/24 ,  C02F1/32 ,  C02F1/44 ,  C02F9/00 ,  C02F9/02 ,  C02F9/12 ,  C02F9/14 ,  C02F11/12 ,  C02F11/14 ,  C02F11/18 ,  C05B5/00 ,  C10J3/06 ,  C10J3/46 ,  C10L5/42

CPC classification number: C02F11/123 ,  B01D61/025 ,  C02F1/001 ,  C02F1/02 ,  C02F1/24 ,  C02F1/32 ,  C02F1/40 ,  C02F1/441 ,  C02F9/00 ,  C02F11/10 ,  C02F11/121 ,  C02F11/18 ,  C02F2103/20 ,  C02F2209/005 ,  C02F2209/02 ,  C02F2209/03 ,  C05B5/00 ,  C10J3/06 ,  C10J3/463 ,  C10J2300/0903 ,  C10J2300/0916 ,  C10J2300/0923 ,  C10J2300/0946 ,  C10J2300/169 ,  C10L5/42 ,  Y02E50/10 ,  Y02E50/30

Abstract: Methods and systems for processing animal waste are disclosed. Effluent, including waste solids and water, is received. The effluent is at least partly separated into solids and water. The separated water is processed using a dissolved air flotation device and/or a reverse osmosis system to clarify the separated water. The separated solids are transferred to a gasifier, which processed the separated solids to form a least a first gas.

Abstract translation: 公开了处理动物废物的方法和系统。 收到包括废物固体和水在内的废水。 流出液至少部分分离成固体和水。 使用溶解的空气浮选装置和/或反渗透系统处理分离的水以澄清分离的水。 将分离的固体转移到气化器中，该气化器处理分离的固体以形成至少第一气体。

公开(公告)号：US5797332A

公开(公告)日：1998-08-25

申请号：US514117

申请日：1995-08-11

Applicant: Michael R. Keller ,  John R. Petersen ,  David Caffey

Inventor： Michael R. Keller ,  John R. Petersen ,  David Caffey

IPC: C10J3/06 ,  F23G5/027 ,  F23G5/16 ,  F23G5/44 ,  F23G7/06 ,  F23G7/10 ,  F26B23/02 ,  F23D14/00

CPC classification number: C10J3/06 ,  C10J3/005 ,  C10K1/024 ,  C10K1/101 ,  F23G5/027 ,  F23G5/16 ,  F23G5/442 ,  F23G7/065 ,  F23G7/105 ,  F26B23/022 ,  C10J2200/158 ,  C10J2300/0909 ,  C10J2300/092 ,  C10J2300/1606 ,  C10J2300/1869 ,  C10J2300/1876 ,  F23G2201/30 ,  F23G2201/303 ,  F23G2202/30 ,  F23G2203/20 ,  F23G2205/121 ,  F23G2206/10 ,  Y02P20/129

Abstract: A system for reducing volatile organic compounds, particulates and carbon monoxide in exhaust from a wood products dryer is disclosed. The dryer exhaust is combined with waste wood or biomass fuel and partially combusted in a rotary gasifier, then fully combusted in a secondary combustion chamber. Hot flue gasses form the secondary combustion chamber are used to heat the conduits carrying the exhaust from the dryer, to heat oil, and to preheat air input to the dryer.

Abstract translation: 公开了一种用于从木制品干燥器中减少废气中的挥发性有机化合物，颗粒和一氧化碳的系统。 干燥器排气与废木材或生物质燃料组合，并在旋转式气化器中部分燃烧，然后在二次燃烧室中完全燃烧。 形成二次燃烧室的热烟道气用于加热承载来自干燥器的排气的管道，加热油，并预热输入到干燥器的空气。