公开(公告)号：US2822820A

公开(公告)日：1958-02-11

申请号：US54100955

申请日：1955-10-17

申请人： SVENSKA FLAEKTFABRIKEN AB

发明人： GEORG SAMUELSSON EVERT

IPC分类号： C10J3/64 ,  F16K13/02 ,  F24F1/00 ,  F24F11/02 ,  F24F11/04 ,  G05D7/01

CPC分类号： G05D7/0173 ,  C10J3/64 ,  F16K13/02 ,  F24F1/0007 ,  F24F11/74 ,  F24F11/81 ,  Y10T137/7786 ,  Y10T137/86718 ,  Y10T137/87338 ,  Y10T137/87442 ,  Y10T137/87981

公开(公告)号：US20230227738A1

公开(公告)日：2023-07-20

申请号：US18152941

申请日：2023-01-11

申请人： Indian Oil Corporation Limited

发明人： Ponoly Ramachandran PRADEEP ,  Shahil SIDDIQUI ,  Vineeth Venu NATH ,  Darshankumar Manubhai DAVE ,  Mainak SARKAR ,  Satyen Kumar DAS ,  Madhusudan SAU ,  Sankara Sri Venkata RAMAKUMAR

IPC分类号： C10G67/16 ,  C10G31/08 ,  C10G67/02 ,  C10G9/00 ,  C10J3/64 ,  C10G69/14

CPC分类号： C10G67/16 ,  C10G31/08 ,  C10G67/02 ,  C10G9/005 ,  C10J3/64 ,  C10G69/14 ,  C10G2400/20 ,  C10G2400/30 ,  C10G2300/1033 ,  C10G2300/301 ,  C10G2300/4006 ,  C10G2300/4012 ,  C10J2300/0943 ,  C10J2300/164 ,  C10G2300/4025 ,  C10G2300/4081

摘要： The present invention relates to a process and system for complete conversion of crude oils by integrating Desalter unit, Atmospheric and vacuum column, high severity FCC process, Naphtha cracking process, residue slurry hydrocracking process, Delayed coking process, Selective mild hydrocracking aromatic production unit, Dehydrogenation units, Aromatic/olefin recovery section, gasifier unit along with syngas to olefins conversion section.

公开(公告)号：US11365362B2

公开(公告)日：2022-06-21

申请号：US17373030

申请日：2021-07-12

申请人： IFP Energies nouvelles

发明人： Jean-Francois Joly ,  Frederic Feugnet

IPC分类号： C10G69/12 ,  C10B53/02 ,  C10B57/06 ,  C10J3/64

摘要： A device and process for the conversion of aromatic compounds, includes/uses: a unit for the separation of the xylenes suitable for treating a cut comprising xylenes and ethylbenzene and producing an extract comprising para-xylene and a raffinate; an isomerization unit suitable for treating the raffinate and producing an isomerate enriched in para-xylene which is sent to a fractionation train; a pyrolysis unit suitable for treating biomass, producing a pyrolysis effluent feeding, at least partially, the feedstock, and producing a pyrolysis gas comprising CO and H2; a Fischer-Tropsch synthesis reaction section suitable for treating, at least in part, the pyrolysis gas, producing a synthesis effluent sent, at least in part, to the pyrolysis unit.

公开(公告)号：US20200239795A1

公开(公告)日：2020-07-30

申请号：US16652648

申请日：2018-10-12

申请人： Danmarks Tekniske Universitet

发明人： Ulrik Birk HENRIKSEN ,  Jesper AHRENFELDT

IPC分类号： C10K1/04 ,  C10K1/02 ,  C10J3/64 ,  C10K1/32 ,  C10K1/34 ,  C10K3/00 ,  C10J3/72 ,  C10J3/84

摘要： Disclosed is a method for reducing the tar content in pyrolysis gas generated in a pyrolysis reactor (1). The method comprises the steps of: guiding the pyrolysis gas through a filter (2) to remove at least 90% of all the particles in the pyrolysis gas having a particle size down to 7 μ and preferably down to 4 μ from the pyrolysis gas, partially oxidizing the pyrolysis gas in a partial oxidation reactor (3) to remove tar from the pyrolysis gas, and guiding the pyrolysis gas through a coke bed (4) to further remove tar from the pyrolysis gas. Furthermore, a two-stage gasifier (6) is disclosed.

公开(公告)号：US20190334411A1

公开(公告)日：2019-10-31

申请号：US16509753

申请日：2019-07-12

申请人： All Power Labs, Inc.

发明人： James Matthew Mason ,  Bear Kaufmann ,  Nicholas Bindbeutel ,  Julia Hasty ,  Ariel Fisk-Vittori

IPC分类号： H02K7/18 ,  F02D19/06 ,  F16N9/04 ,  F02B63/04 ,  C10J3/26 ,  C10J3/66 ,  C10J3/64 ,  C10B53/02 ,  F02B43/08 ,  F02C7/20 ,  F02C7/22 ,  C10K1/02

摘要： A compact biomass gasification-based power generation system that converts carbonaceous material into electrical power, including an enclosure that encases: a gasifier including a pyrolysis module coaxially arranged above a reactor module, a generator including an engine and an alternator, and a hopper. The generator system additionally includes a first heat exchanger fluidly connected to an outlet of the reactor module and thermally connected to the drying module, a second heat exchanger fluidly connected to an outlet of the engine and thermally connected to the pyrolysis module, and a third heat exchanger fluidly connected between the outlet of the reactor module and the first heat exchanger, the third heat exchanger thermally connected to an air inlet of the reactor module. The system can additionally include a central wiring conduit electrically connected to the pyrolysis module, reactor module, and engine, and a control panel connected to the conduit that enables single-side operation.

公开(公告)号：US10144887B2

公开(公告)日：2018-12-04

申请号：US14662152

申请日：2015-03-18

申请人： CURTIN UNIVERSITY OF TECHNOLOGY

发明人： Chun-Zhu Li ,  Hongwei Wu ,  Mohammad Asadullah ,  Xiaoshan Wang

IPC分类号： C10J3/20 ,  C10J3/64 ,  C10J3/66 ,  C10K3/02 ,  C10J3/32 ,  C10J3/38 ,  C10J3/62 ,  C10J3/72 ,  C10K3/00 ,  C10K3/04 ,  C10B47/06 ,  B01J21/18 ,  B01J23/745 ,  B01J23/755

摘要： A method of gasifying carbonaceous material is described. The method comprises a first step of pyrolyzing and partially gasifying the carbonaceous material to produce volatiles and char. The volatiles and the char are then separated and, subsequently, the char is gasified and the volatiles are reformed. The raw product gas is then finally cleaned with char or char-supported catalysts or other catalysts.

公开(公告)号：US09321640B2

公开(公告)日：2016-04-26

申请号：US14173957

申请日：2014-02-06

申请人： Plasco Energy Group Inc.

发明人： Andreas Tsangaris ,  Marc Bacon

IPC分类号： B01J7/00 ,  C01B3/22 ,  C10J3/48 ,  C10J3/64 ,  C10J3/72 ,  C10J3/82 ,  C10K1/00 ,  C10K3/00 ,  C10J3/42

CPC分类号： C01B3/22 ,  C01B2203/0266 ,  C01B2203/0861 ,  C01B2203/16 ,  C10J3/42 ,  C10J3/48 ,  C10J3/64 ,  C10J3/721 ,  C10J3/723 ,  C10J3/726 ,  C10J3/82 ,  C10J2200/09 ,  C10J2300/0916 ,  C10J2300/093 ,  C10J2300/094 ,  C10J2300/0946 ,  C10J2300/0956 ,  C10J2300/0973 ,  C10J2300/1606 ,  C10J2300/1634 ,  C10J2300/165 ,  C10J2300/1675 ,  C10J2300/1687 ,  C10J2300/1869 ,  C10J2300/1884 ,  C10K1/002 ,  C10K3/001 ,  Y02P20/145

摘要： The invention provides a system designed for the complete conversion of carbonaceous feedstock into syngas and slag. The system comprises a primary chamber for the volatilization of feedstock generating a primary chamber gas (an offgas); a secondary chamber for the further conversion of processed feedstock to a secondary chamber gas (a syngas) and a residue; a gas-reformulating zone for processing gas generated within one or more of the chambers; and a melting chamber for vitrifying residue. The primary chamber comprises direct or indirect feedstock additive capabilities in order to adjust the carbon content of the feedstock.The system also comprises a control system for use with the gasification system to monitor and regulate the different stages of the process to ensure the efficient and complete conversion of the carbonaceous feedstock into a syngas product.

摘要翻译： 本发明提供了一种设计用于将碳质原料完全转化成合成气和渣的系统。 该系统包括用于挥发原料产生初级室气体（废气）的主室; 用于将经处理的原料进一步转化为二次室气体（合成气）和残余物的二级室; 用于处理在一个或多个室内产生的气体的气体重整区; 和用于玻璃化残渣的熔化室。 主室包括直接或间接的原料添加剂能力，以调节原料的碳含量。 该系统还包括与气化系统一起使用的控制系统，以监测和调节该过程的不同阶段，以确保碳质原料有效和完全转化为合成气产品。

公开(公告)号：US09279089B2

公开(公告)日：2016-03-08

申请号：US13876015

申请日：2011-10-05

申请人： Li Chen ,  Anthony Kerihuel ,  Luc Gerun

发明人： Li Chen ,  Anthony Kerihuel ,  Luc Gerun

IPC分类号： C10J3/84 ,  C10J3/74 ,  C10J3/64 ,  C10B51/00 ,  F23G5/24 ,  F23G7/10 ,  C10B53/02 ,  F23G5/027

CPC分类号： C10J3/84 ,  C10B51/00 ,  C10B53/02 ,  C10J3/64 ,  C10J3/74 ,  C10J2300/0909 ,  C10J2300/1606 ,  C10J2300/1807 ,  F23G5/027 ,  F23G5/24 ,  F23G7/10 ,  F23G2201/301 ,  F23G2201/303 ,  F23G2201/304 ,  F23G2205/16 ,  F23G2209/262 ,  F23G2209/28 ,  Y02E50/14

摘要： A device for converting a fuel including solid components, known as a solid fuel, into a gaseous fuel, includes a pyrolysis zone (2) for pyrolyzing solid fuel, having pyrolysis elements that are capable of decomposing the solid fuel into a pyrolysis gas and into a solid pyrolysis residue, known as coke, and a combustion zone (3), which is distinct from the pyrolysis zone (2), for burning the pyrolysis gas and having combustion elements (31, 32, 33). The device also includes elements for circulating pyrolysis gas from the pyrolysis zone (2) to the combustion zone (3), which is surrounded by the pyrolysis zone (2).

摘要翻译： 用于将包含固体成分（称为固体燃料）的燃料转化为气体燃料的装置包括用于热解固体燃料的热解区（2），其具有能够将固体燃料分解成裂解气体的热解元素 称为焦炭的固体热解残渣和与热解区（2）不同的燃烧区（3），用于燃烧热解气并具有燃烧元件（31,32,33）。 该装置还包括用于将热解气体从热解区（2）循环到由热解区（2）包围的燃烧区（3）的元件。

公开(公告)号：US5573559A

公开(公告)日：1996-11-12

申请号：US546294

申请日：1995-10-20

申请人： Wesley P. Hilliard ,  Scott Barney

发明人： Wesley P. Hilliard ,  Scott Barney

IPC分类号： C10J3/20 ,  C10J3/42 ,  C10J3/64 ,  C10J3/14

CPC分类号： C10J3/20 ,  C10J3/42 ,  C10J3/64 ,  C10J3/721 ,  C10J3/723 ,  C10J3/80 ,  C10K1/02 ,  C10J2300/0906 ,  C10J2300/0946 ,  C10J2300/1606 ,  C10J2300/1884

摘要： Apparatus and method for gasification of waste are disclosed. Waste material is fed to the top of a first combustion chamber, and a burning, rotating annular column of waste is supported in the combustion chamber. Combustion air is introduced to the first combustion chamber at or below the support for the burning annular column of waste so that the combustion air moves upwardly through the burning column. Combustion gases are withdrawn from the top portion of the first combustion chamber. Particulates are removed and recirculated to the first combustion chamber. The combustion gases are then fed to the top portion of a second combustion chamber. Secondary combustion air and optional fuel are fed to the second combustion chamber to complete the gasification process. A relatively clean producer gas is withdrawn from the bottom portion of the secondary combustion chamber.

摘要翻译： 公开了废气气化装置和方法。 废料被供给到第一燃烧室的顶部，并且燃烧的旋转环形废物列被支撑在燃烧室中。 燃烧空气被引入到用于燃烧环形废物列的支撑件的下方或下方的第一燃烧室，使得燃烧空气向上移动通过燃烧塔。 燃烧气体从第一燃烧室的顶部排出。 颗粒被去除并再循环到第一燃烧室。 然后将燃烧气体送入第二燃烧室的顶部。 二次燃烧空气和任选的燃料被供给到第二燃烧室以完成气化过程。 相对清洁的发生器气体从二级燃烧室的底部排出。

公开(公告)号：US5484465A

公开(公告)日：1996-01-16

申请号：US222625

申请日：1994-04-04

申请人： Wesley P. Hilliard ,  Scott Barney

发明人： Wesley P. Hilliard ,  Scott Barney

IPC分类号： C10J3/20 ,  C10J3/42 ,  C10J3/64

CPC分类号： C10J3/20 ,  C10J3/42 ,  C10J3/64 ,  C10J3/721 ,  C10J3/723 ,  C10J3/80 ,  C10K1/02 ,  C10J2300/0906 ,  C10J2300/0946 ,  C10J2300/1606 ,  C10J2300/1884

摘要： Apparatus and method for gasification of waste are disclosed. Waste material is fed to the top of a first combustion chamber, and a burning, rotating annular column of waste is supported in the combustion chamber. Combustion air is introduced to the first combustion chamber at or below the support for the burning annular column of waste so that the combustion air moves upwardly through the burning column. Combustion gases are withdrawn from the top portion of the first combustion chamber. Particulates are removed and recirculated to the first combustion chamber. The combustion gases are then fed to the top portion of a second combustion chamber. Secondary combustion air and optional fuel are fed to the second combustion chamber to complete the gasification process. A relatively clean producer gas is withdrawn from the bottom portion of the secondary combustion chamber.

摘要翻译： 公开了废气气化装置和方法。 废料被供给到第一燃烧室的顶部，并且燃烧的旋转环形废物列被支撑在燃烧室中。 燃烧空气被引入到用于燃烧环形废物列的支撑件的下方或下方的第一燃烧室，使得燃烧空气向上移动通过燃烧塔。 燃烧气体从第一燃烧室的顶部排出。 颗粒被去除并再循环到第一燃烧室。 然后将燃烧气体送入第二燃烧室的顶部。 二次燃烧空气和任选的燃料被供给到第二燃烧室以完成气化过程。 相对清洁的发生器气体从二级燃烧室的底部排出。