公开(公告)号：US11802251B2

公开(公告)日：2023-10-31

申请号：US17651185

申请日：2022-02-15

Applicant: Eastman Chemical Company

Inventor： William Lewis Trapp ,  Justin William Murphy ,  Nathan Mitchell West

IPC: C10J3/48 ,  C10J3/00 ,  C10J3/46 ,  C10J3/50

CPC classification number: C10J3/485 ,  C10J3/002 ,  C10J3/466 ,  C10J3/506 ,  C10J2300/092 ,  C10J2300/093 ,  C10J2300/0906 ,  C10J2300/0923 ,  C10J2300/0943 ,  C10J2300/0946 ,  C10J2300/0953 ,  C10J2300/0959 ,  C10J2300/0973 ,  C10J2300/164 ,  C10J2300/1665 ,  C10J2300/1846 ,  Y02P20/143

Abstract: Pre-ground plastics of small particle size not more than 2 mm are co-fed into a solid fossil fuel fed entrained flow partial oxidation gasifier. A syngas composition can be made by charging an oxidant and a feedstock composition comprising recycle plastics and a solid fossil fuel to a gasification zone within a gasifier; gasifying the feedstock composition together with the oxidant in said gasification zone to produce said syngas composition; and discharging at least a portion of said syngas composition from said gasifier; wherein the recycled plastics are added to a feed point comprising a solid fossil fuel belt feeding a grinder after the solid fossil fuel is loaded on the belt, a solid fossil fuel belt feeding a grinder before the solid fossil fuel is loaded onto the belt, or a solid fossil fuel slurry storage tank containing a slurry of said solid fossil fuel ground to a size as the size fed to the gasification zone.

公开(公告)号：US20230287285A1

公开(公告)日：2023-09-14

申请号：US18139447

申请日：2023-04-26

Applicant: Frichs Holding 2 ApS

Inventor： Ove KUDAHL MUNCH

IPC: C10J3/48 ,  C10J3/46 ,  C10J3/50 ,  C10J3/74 ,  C10J3/52

CPC classification number: C10J3/485 ,  C10J3/466 ,  C10J3/506 ,  C10J3/74 ,  C10J3/526 ,  C10J2300/092 ,  C10J2300/1246 ,  C10J2300/1823 ,  C10J2300/1884 ,  C10J2200/152 ,  C10J2200/158 ,  C10J2200/09

Abstract: Methods and pyrolysis plants are described, comprising reactors for producing pyrolysis gas from biomass. The reactors comprise one or more reaction channels linked thermally with at least one heating circuit, which is configured to heat the reaction channels to a temperature that is high enough to gasify the biomass. The reactors comprise a feed section configured for feeding the biomass into the reaction channels. The pyrolysis plants comprise a gas accelerator configured for recirculating the gas that is present in the at least one reaction channel and for providing a gas flow velocity that is able to distribute the biomass in the reaction channel.

公开(公告)号：US11718803B2

公开(公告)日：2023-08-08

申请号：US17270586

申请日：2019-11-07

Applicant: Mitsubishi Power, Ltd.

Inventor： Yuta Konagayoshi ,  Makoto Toyomaru ,  Kengo Muroya ,  Fumihiro Chuman

IPC: C10J3/76 ,  C10J3/48 ,  F23M5/08

CPC classification number: C10J3/76 ,  C10J3/485 ,  C10J2200/09 ,  C10J2300/1223 ,  C10J2300/1653

Abstract: A cooling wall includes: a wall surface defined by arrangement of central axes of a plurality of cooling tubes; and an opening formed in a part of the wall surface in which a burner is installable, each of the plurality of cooling tubes forming the opening has a straight portion and a curved portion, the plurality of cooling tubes include a first cooling tube whose first virtual axis extending in an axial direction of the straight portion overlaps the opening, and a second cooling tube whose second virtual axis extending in an axial direction of the straight portion is located outside an outer circumference of the opening in a radial direction, the curved portion of the first cooling tube is arranged so as to form a curve along the outer circumference surface of the opening and on a surface along the wall surface.

公开(公告)号：US10072841B2

公开(公告)日：2018-09-11

申请号：US13522914

申请日：2011-01-20

Applicant: Mikael Rüdlinger

Inventor： Mikael Rüdlinger

IPC: F23J15/00 ,  F02M25/03 ,  C10J3/06 ,  C10J3/48 ,  C10J3/66 ,  C10K1/04

CPC classification number: F23J15/006 ,  C10J3/485 ,  C10J3/66 ,  C10J2300/0969 ,  C10K1/04 ,  F02M25/03 ,  Y02T10/121

Abstract: A device (1) for performing mechanical work and/or producing electrical or thermal energy, the energy necessary for operation is obtained from the oxidation of carbonaceous fuels (20) into carbon dioxide (24) and water (23). The device comprises means (14) for compression and/or condensation of the exhaust gas (21), and storage means (15) for receiving the compressed and/or condensed exhaust gas (21).

公开(公告)号：US10035963B2

公开(公告)日：2018-07-31

申请号：US15398394

申请日：2017-01-04

Applicant: RES USA, LLC

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

IPC: C10J3/46 ,  C01B3/02 ,  C10G2/00

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 ,  Y02P30/30

Abstract: A mixing apparatus for producing a feedstock for a reformer, the mixing apparatus including at least one mixing vessel comprising a cylindrical vessel with a conical bottom; a steam inlet configured for introducing steam into the conical bottom; a carbonaceous material inlet configured for introducing a carbonaceous feed into the cylindrical vessel; and an outlet for a reformer feedstock comprising at least 0.3 pounds of steam per pound of carbonaceous material, with the at least one mixing vessel configured for operation at a pressure of greater than about 10 psig.

公开(公告)号：US20180195015A1

公开(公告)日：2018-07-12

申请号：US15811662

申请日：2017-11-13

Applicant: BEIJING QING CHUANG JIN HUA TECHNOLOGY CO., LTD.

Inventor： Hongbo MA ,  Jun YUE ,  Shuai WANG

IPC: C10J3/86 ,  C10J3/82 ,  C10J3/56 ,  C10J3/52 ,  C10J3/72 ,  F28D21/00

CPC classification number: C10J3/86 ,  C10J3/485 ,  C10J3/52 ,  C10J3/56 ,  C10J3/723 ,  C10J3/76 ,  C10J3/82 ,  C10J3/845 ,  C10J2300/0936 ,  C10J2300/0976 ,  F22B1/1846 ,  F28D21/001 ,  Y02P20/129

Abstract: The present disclosure relates to a constant liquid level gasification furnace with a waste boiler comprising: a housing; an upper portion of the housing is defined as a gasification section, a middle portion of the housing is defined as a radiant section, and a lower portion of the housing is defined as a quenching section. The gasification section internally includes a membrane type water-cooled wall, wherein the inner region defined by the membrane type water-cooled wall is a gasification chamber. The radiant section internally includes a built-in radiant waste boiler assembly, wherein the internal region defined by the built-in radiant waste boiler assembly is a radiant chamber. The region defined by the quenching section is a quenching chamber.

公开(公告)号：US20170275544A1

公开(公告)日：2017-09-28

申请号：US15080043

申请日：2016-03-24

Applicant: General Electric Company

Inventor： Thomas Frederick Leininger

IPC: C10J3/72 ,  C01B3/02 ,  C10J3/84 ,  C10K1/02 ,  C10J3/48 ,  C10J3/46

CPC classification number: C10J3/721 ,  C01B3/02 ,  C10J3/466 ,  C10J3/485 ,  C10J3/84 ,  C10J2300/0906 ,  C10J2300/093 ,  C10J2300/0959 ,  C10J2300/1823 ,  C10K1/026

Abstract: A system includes a first reactor that may gasify a first feed to generate a first syngas. The first feed has a first particle size distribution (PSD1). The system also includes a second reactor that may receive the first feed, a second feed, and at least a portion of the first syngas. The second reactor may gasify the second feed to generate additional syngas, and the second feed has a second particle size distribution (PSD2) that is different from the first PSD. The second reactor includes an elutriation zone disposed on a first end of the second reactor. The elutriation zone may receive the first and second feed. The second reactor also includes a fluidized bed disposed at a second end of the second reactor that is substantially opposite the first end. The fluidized bed is fluidly coupled to the first reactor and may receive the portion of the first syngas via a syngas inlet. The system also includes a gas-solids separation section fluidly coupled to the first and second reactors. The gas-solids separation section may receive the first feed and partially reacted particles of the second feed from the elutriation zone and may feed a combined feed consisting of the first feed and the partially reacted particles of the second feed to the first reactor.

公开(公告)号：US09766133B2

公开(公告)日：2017-09-19

申请号：US14079065

申请日：2013-11-13

Applicant: Lummus Technology Inc.

Inventor： Steven Elmer Chichester ,  Michael James Hickey

IPC: G01K1/08 ,  G01K1/12 ,  G01K1/14 ,  C10J3/48 ,  C10J3/72 ,  C10J3/86 ,  C10K1/00 ,  C10K1/02 ,  C10K3/04

CPC classification number: G01K1/14 ,  C10J3/485 ,  C10J3/721 ,  C10J3/723 ,  C10J3/86 ,  C10J2300/0906 ,  C10J2300/093 ,  C10J2300/0943 ,  C10J2300/0959 ,  C10J2300/0973 ,  C10J2300/1612 ,  C10J2300/165 ,  C10J2300/1653 ,  C10J2300/1675 ,  C10J2300/1884 ,  C10K1/003 ,  C10K1/024 ,  C10K3/04 ,  Y02E20/18 ,  Y02E20/185

Abstract: A temperature measurement system for a gasifier may employ a first stage gasifier with a refractory wall that defines a first stage gasifier volume. A protruding refractory brick may protrude from the first stage refractory wall and into a gaseous flow path of the first stage gasifier volume. The temperature sensor may reside completely through the refractory wall, which may be a plurality of brick layers, except for a tip end of a temperature sensor that may reside in a blind or non-through hole within the protruding refractory brick. The protruding refractory brick protrudes beyond a normal wall surface of the plurality of brick layers that defines the first stage gasifier volume. The protruding refractory brick may have a face that forms an angle that is not 90 degrees, such as 45 degrees, relative to the gaseous flow path of the fluid stream through the first stage gasifier volume.

公开(公告)号：US20170218286A1

公开(公告)日：2017-08-03

申请号：US15492427

申请日：2017-04-20

Applicant: GENSOS HOLDING B.V.

Inventor： John HARINCK ,  Klaas Gerrit SMIT

IPC: C10J3/84 ,  C10J3/48 ,  C10K1/02 ,  C10J3/20

CPC classification number: C10J3/84 ,  C10J3/20 ,  C10J3/485 ,  C10J3/78 ,  C10J3/86 ,  C10J2300/0916 ,  C10J2300/0923 ,  C10J2300/0979 ,  C10J2300/1223 ,  C10J2300/1246 ,  C10J2300/1884 ,  C10K1/026 ,  C10L9/086 ,  Y02E50/14

Abstract: A process for the gasification of wet biomass. The process comprises heating wet biomass at a pressure in the range of from 22.1 MPa to 35 MPa. The wet biomass is heated from a temperature of at most T1 to a temperature of at least T2 by heat exchange with a first heating fluid. The gasification product is further heated. The further heated gasification product is used as the first heating fluid, upon which the further heated gasification product is cooled down from a temperature of at least T3 to a temperature of at most T4. The temperatures T1, T2, T3 and T4 can be calculated by using certain mathematical formulae. Also claimed: a reaction apparatus for the gasification of wet biomass.

公开(公告)号：US20170130148A1

公开(公告)日：2017-05-11

申请号：US15218068

申请日：2016-07-24

Applicant: Synthesis Energy Systems, Inc.

Inventor： Francis Sikming Lau

IPC: C10J3/52 ,  C10J3/72 ,  C01B3/02 ,  C10J3/48

CPC classification number: C10J3/526 ,  C01B3/02 ,  C10J3/485 ,  C10J3/523 ,  C10J3/723 ,  C10J2300/093 ,  F23C10/24 ,  F23C10/26 ,  F23C10/30 ,  F23C2900/10008 ,  F23J1/00 ,  F23J2900/01006

Abstract: A fluidized bed gasification system which comprises a fluidized bed gasification reactor having a bottom ash discharge outlet below the reactor, wherein an L-valve is used to control the rate of bottom ash discharge. The L-valve uses an aeration port located on distal side of the L-valve vertical pipe at a location that is above the center line of the horizontal pipe. Also provided are methods of controlling the bottom ash discharge as well the fluidized reaction bed height of the system.