-
公开(公告)号：US20240010919A1
公开(公告)日：2024-01-11
申请号：US18156930
申请日：2023-01-19
申请人： Arnold Keller , Michael Keller
发明人： Arnold Keller , Michael Keller
IPC分类号： C10G1/04 , C01B3/12 , C01B3/50 , C01B32/50 , B01J19/24 , C10L3/08 , C10L1/02 , C11C3/10 , C07C29/147 , C10J3/84 , C12M1/00
CPC分类号： C10G1/045 , C01B3/12 , C01B3/50 , C01B32/50 , B01J19/245 , C10L3/08 , C10L1/026 , C11C3/10 , C07C29/147 , C10J3/84 , C12M21/12 , C12M43/02 , C01B2203/0283 , C01B2203/0883 , C01B2203/0475 , C10L2200/0476 , C10L2290/04 , C10L2290/06 , C10J2300/0906 , C10J2300/1675 , C10J2300/1612 , C10L2290/10 , C10J2300/0916 , C10J2300/1884 , C10J2300/1681 , C10J2300/1643 , C10L2270/026 , C10G2300/1011 , C10G2300/4006 , C10G2300/4043
摘要： A system and method of producing synthesis gas and bio-oil from biomass. The method comprises producing, in a gasification unit, synthesis gas from a carbonaceous feedstock, optionally cooling the synthesis gas discharged from the gasification unit, channeling the synthesis gas towards a hydrothermal processing unit, wherein the hydrothermal processing unit is configured to process a biomass feedstock contained in a pressurized water stream, transferring, in the hydrothermal processing unit, heat from the synthesis gas to the biomass feedstock, and producing a hydrothermal product from the biomass feedstock in the pressurized water stream.
-
公开(公告)号：US20180354006A1
公开(公告)日：2018-12-13
申请号：US16061885
申请日：2016-12-16
发明人： Anne BENICHOU , Annie LAGOUTTE , Xavier MAURANCE , Jacques PROOT
CPC分类号： B09B3/005 , B09B3/00 , B09B3/0025 , B09B3/0066 , B09B5/00 , C10J3/00 , C10J2300/09 , C10J2300/1618 , C10J2300/1884 , F23G5/0276 , F23G5/085 , F23G5/12 , F23G5/165 , F23G5/46 , F23G2200/00 , F23G2202/50 , F23G2206/203 , Y02E20/12
摘要： The present invention relates to a method and a plant for treating carbon-containing waste that may comprise mineral fillers and/or potential contaminants.This method comprises: preparing a molten glass bath at a temperature between 1100° C. and 1600° C.; loading the waste to be treated into said molten glass bath; injecting an oxidizer and optionally a fuel under pressure into said molten glass bath by means of at least one hose, one end of which is immersed in said bath, said oxidizer being introduced in a molar amount less than the molar amount of the carbon-containing compounds, thus causing combustion of said waste and generation of hot synthesis gases; implementing heat exchange between a heat-transfer fluid and the hot synthesis gases in conditions allowing simultaneous recovery of at least part of their heat energy and at least part of the heat energy released by their combustion, air being injected sequentially into said gases during said heat exchange to cause self-ignition of the mixture of said gases and air, each injection increasing the degree of combustion.
-
公开(公告)号：US20180320094A1
公开(公告)日：2018-11-08
申请号：US15773345
申请日：2016-11-04
申请人： HAFFNER ENERGY
CPC分类号： C10J3/66 , C01B3/02 , C10J2300/0916 , C10J2300/1884 , C10K1/02 , C10K1/04 , Y02P20/145
摘要： A method for producing a synthesis gas from an organic material with a moisture content of less than 20%. A first step for carrying out the thermolysis of the organic material and a second, separate step for the gasification (ii) of the thermolysed organic material. The thermolysis step is carried out by increasing the temperature of the raw material up to an end temperature higher than 150° C. and lower than 1400° C.; —the thermolysis step (i) is carried out in a controlled gas atmosphere in which the quantity of oxygen supplied is less than 20% of the quantity of oxygen required for the stoichiometric combustion of the organic raw material; —the thermolysis gas obtained in the thermolysis step is conveyed to a purification step (iii) for removing undesirable elements.
-
公开(公告)号：US20180119949A1
公开(公告)日：2018-05-03
申请号：US15565602
申请日：2016-04-11
IPC分类号： F23G5/08 , B09B3/00 , C02F11/18 , C02F11/10 , C10J3/18 , F23G5/027 , F23G5/16 , F23G5/46 , B09C1/06
CPC分类号： F23G5/085 , B09B3/0083 , B09C1/067 , C02F11/10 , C02F11/18 , C02F2103/10 , C03B37/055 , C10J3/18 , C10J2300/0946 , C10J2300/1238 , C10J2300/1653 , C10J2300/1884 , F02B43/10 , F02B63/04 , F23G5/0276 , F23G5/16 , F23G5/46 , F23G2201/303 , F23G2204/201 , F23G2209/101 , F23G2209/102 , F23G2900/7013 , Y02E20/16 , Y02E20/18 , Y02P20/129
摘要： A system comprising a plasma assisted vitrifier (8) configured to produce vitrified product. A feed pipe (4) can be fluidly connected to the plasma assisted vitrifier (8). The feed pipe (4) can be configured to deliver a feedstock into the plasma assisted vitrifier. A heated combustion air conduit (34) can be fluidly connected to the plasma assisted vitrifier (8). A spinning fiberizer can be disposed next to the plasma assisted vitrifier (8) and configured to receive the vitrified product (24). An emissions attenuation device can be fluidly connected to the plasma-assisted vitrifier (8) and configured to treat gaseous emissions generated by the plasma-assisted vitrifier (8).
-
公开(公告)号：US09957444B2
公开(公告)日：2018-05-01
申请号：US15102743
申请日：2014-12-16
申请人： Renergi Pty Ltd
发明人： Chun-Zhu Li , Richard Gunawan , Li Dong
CPC分类号： C10B47/32 , C10B5/20 , C10B51/00 , C10B53/02 , C10J3/66 , C10J2300/0909 , C10J2300/0916 , C10J2300/094 , C10J2300/1884 , C10K1/32 , C10L9/083 , Y02E50/14 , Y02E50/15
摘要： An apparatus for pyrolyzing a carbonaceous material and producing char and volatiles includes a vessel having an inlet for the carbonaceous material, an outlet for the char and the volatiles, and a first pathway therebetween. The vessel has wall portions with interior surfaces that define the first pathway. Further, the vessel has a heat exchange medium inlet, outlet and a second pathway therebetween. The first and second pathways are in heat exchange proximity to each other and the second pathway is defined by interior surfaces of the, or other, wall interior portions of the vessel. At least some of the interior wall portions of the vessel project into an interior space of the vessel such that at least one of the first and second pathways is non-linear.
-
公开(公告)号：US09926501B2
公开(公告)日：2018-03-27
申请号：US14898262
申请日：2014-06-02
CPC分类号： C10J3/485 , C10J3/08 , C10J3/466 , C10J3/76 , C10J2300/0956 , C10J2300/0976 , C10J2300/1884 , C10J2300/1892
摘要： An entrained-flow gasifier reactor includes a vessel and a first liner within the vessel. The first liner extends around a reaction zone in the vessel and has an inlet end and an exit end with respect to the reaction zone. The first liner includes a drip lip at the exit end. An isolator is arranged near the drip lip. The isolator is operable to thermally isolate the drip lip from a quench zone downstream from the reaction zone such that molten slag at the drip lip remains molten.
-
公开(公告)号：US09822319B2
公开(公告)日：2017-11-21
申请号：US15011644
申请日：2016-01-31
发明人： Yilong Chen , Yanfeng Zhang , Hongming Tang
CPC分类号： C10J3/84 , C10J3/20 , C10J3/46 , C10J2200/152 , C10J2300/0906 , C10J2300/0916 , C10J2300/0973 , C10J2300/0976 , C10J2300/1238 , C10J2300/1246 , C10J2300/1653 , C10J2300/1659 , C10J2300/1665 , C10J2300/1693 , C10J2300/1853 , C10J2300/1884 , C10J2300/1892 , C10K1/002 , C10K1/003 , C10K1/02 , C10K1/06 , Y02E20/18 , Y02E50/14 , Y02E50/18 , Y02P20/145
摘要： A system for gasifying biomass is disclosed. The system comprises a water storage tank, a water pump, a heat exchanger, a plasma torch heater, a gasifier, an ash cooler, a spray tower, a dust collector, a deacidification tower, and a desiccator. The water storage tank is connected to the water inlet of the heat exchanger; the vapor outlet of the heat exchanger is connected to the vapor inlet of the plasma torch heater; the vapor outlet of the plasma torch heater is connected to the vapor nozzle of the gasifier; the ash outlet of the gasifier is connected to the ash inlet of the ash cooler; the gas outlet of the gasifier is connected to the gas inlet of the spray tower; and the gas outlet of the spray tower is connected to the gas inlet of the heat exchanger.
-
公开(公告)号：US09683184B2
公开(公告)日：2017-06-20
申请号：US13912034
申请日：2013-06-06
CPC分类号： C10J3/723 , C10J2300/0906 , C10J2300/0909 , C10J2300/0969 , C10J2300/0976 , C10J2300/165 , C10J2300/1653 , C10J2300/1675 , C10J2300/1687 , C10J2300/1815 , C10J2300/1876 , C10J2300/1884 , C10J2300/1892 , Y02E20/16 , Y02E20/18 , Y02P20/13
摘要： A gasification system includes a gasifier configured to gasify a feedstock and an oxidant to generate a producer gas, a steam generator configured to supply steam to the gasifier, and a combustion system configured to supply an exhaust gas to the steam generator to produce the steam. The system also includes an exhaust gas injection system located upstream of the gasifier and fluidly coupled to the gasifier. The exhaust gas injection system is configured to supply a portion of the exhaust gas from the combustion system to the gasifier.
-
公开(公告)号：US09657243B2
公开(公告)日：2017-05-23
申请号：US14239630
申请日：2012-08-20
申请人： John Harinck , Klaas Gerrit Smit
发明人： John Harinck , Klaas Gerrit Smit
CPC分类号： 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
摘要： 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：US09605220B2
公开(公告)日：2017-03-28
申请号：US14692633
申请日：2015-04-21
IPC分类号： B01J7/00 , C10J3/84 , C10J3/82 , C10K1/00 , C10K1/02 , C10K1/10 , B01J19/00 , B01J19/24 , C10J3/20 , F01K25/10 , C10K1/04 , C10J3/00 , C10J3/80
CPC分类号： C10J3/84 , B01D3/007 , B01J19/0006 , B01J19/24 , B01J2219/00103 , B01J2219/24 , C10J3/00 , C10J3/20 , C10J3/80 , C10J3/82 , C10J2200/00 , C10J2200/09 , C10J2300/169 , C10J2300/1861 , C10J2300/1869 , C10J2300/1884 , C10J2300/1892 , C10K1/003 , C10K1/02 , C10K1/046 , C10K1/10 , C10K1/101 , F01K25/10 , Y02E20/18 , Y02P20/124 , Y02P20/129 , Y02P30/10
摘要： Energy-efficient gasification-based multi-generation apparatus, facilities, or systems, and methods of modifying existing gasification-based multi-generation apparatus and the various conventional thermal coupling arrangements, are provided. An exemplary gasification-based multi-generation apparatus includes a gasification system configured to generate raw syngas feed from a carbon-based feedstock, and an acid gas removal system configured to remove acidic contaminants from the raw syngas feed to thereby provide a treated syngas feed. The gasification system includes a gasification reactor, a syngas fluid cooler reactor, and a soot ash removal unit comprising a soot quench column, a soot separator, a soot filter, a soot scrubber, and a gasification system energy management system having a conventional set of heat exchanger unit and an added set of heat exchanger units to enhance energy efficiency. The acid gas removal system includes a reactor, an acid gas contaminant absorber, a solvent regenerator, and an acid gas removal system energy management system having a conventional set of heat exchanger unit and an added set of heat exchanger units to enhance energy efficiency.
-
-
-
-
-
-
-
-
-
搜索结果
944 条记录 (耗时 0.029 秒)
