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公开(公告)号：US10221360B2
公开(公告)日：2019-03-05
申请号：US15831358
申请日：2017-12-04
发明人： Daxiang Wang , Pingyu Kuai , Meng Li , Yanfeng Zhang
IPC分类号： C10G2/00 , C10K1/00 , C10K1/12 , C01B3/04 , C01B3/52 , C10J3/84 , C10J3/48 , C10J3/00 , C10K1/32
摘要： A method for Fischer-Tropsch synthesis, the method including: 1) gasifying a raw material to obtain a crude syngas including H2, CO and CO2; 2) electrolyzing a saturated NaCl solution using a chloralkali process to obtain a NaOH solution, Cl2 and H2; 3) removing the CO2 in the crude syngas using the NaOH solution obtained in 2) to obtain a pure syngas; and 4) insufflating the H2 obtained in 2) to the pure syngas to adjust a mole ratio of CO/H2 in the pure syngas, and then introducing the pure syngas for Fischer-Tropsch synthesis reaction. A device for Fischer-Tropsch synthesis includes a gasification device, an electrolyzer, a first gas washing device, and a Fischer-Tropsch synthesis reactor.
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公开(公告)号：US20180371339A1
公开(公告)日：2018-12-27
申请号：US16062292
申请日：2016-12-15
申请人： Shell Oil Company
发明人： Sijing LIU , Manfred Heinrich SCHMITZ-GOEB , Anthony WOLFERT , Unai JAUREGI , Joachim Ottomar WOLFF
摘要： A gasification system for the oxidation of a carbonaceous feedstock to provide a synthesis gas comprising: a reactor chamber for oxidizing the carbonaceous feedstock; a quench section for holding a bath of liquid coolant; an intermediate section having a reactor outlet opening through which the synthesis gas is conducted from the reactor chamber into the bath of the quench section; at least one layer of refractory bricks arranged on the reactor chamber floor, the lower end section of the refractory brick enclosing the reactor outlet opening and defining the inner diameter thereof; the intermediate section including a number of halved tubes for liquid coolant arranged onto at least part of the reactor chamber floor on a side thereof opposite to the lower end section of the refractory bricks; and a pump system for circulating the liquid coolant through the halved tubes on the reactor chamber floor.
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公开(公告)号：US10144888B2
公开(公告)日：2018-12-04
申请号：US15492427
申请日：2017-04-20
申请人： GENSOS HOLDING B.V.
发明人： John Harinck , Klaas Gerrit Smit
IPC分类号： C10J3/84 , C10J3/48 , C10K1/02 , C10J3/20 , C10J3/78 , C10L9/08 , C10J3/86 , C10B53/07 , B09B3/00
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.
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公开(公告)号：US10131855B2
公开(公告)日：2018-11-20
申请号：US15167997
申请日：2016-05-28
发明人： Yanfeng Zhang , Liang Zhang , Yilong Chen
摘要： A method for pressurized pyrolysis of biomass in a pressurized pyrolysis furnace, including: 1) crushing and screening biomass; collecting biomass having desired particle sizes; and delivering the biomass having desired particle sizes to a pulse-type feeding system; 2) transporting the biomass to a pyrolysis furnace via the pulse-type feeding system; synchronously initiating microwave and a plasma torch, the microwave producing a microwave field in the pyrolysis furnace, working gas of the plasma torch being ionized for the first time to produce plasma jet entering the pyrolysis furnace; and 3) allowing the syngas generated in 2) to continue moving upwards and introducing the syngas out from the top of the pyrolysis furnace; chilling the syngas; introducing the syngas to a cyclone separator to separate residues; and then cooling and purifying the syngas using a cooling device and a purifying device, respectively, to produce clean syngas.
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公开(公告)号：US20180223201A1
公开(公告)日：2018-08-09
申请号：US15429099
申请日：2017-02-09
CPC分类号： C10J3/845 , B01D45/08 , B01D47/021 , B01D50/004 , C10J2300/1603 , F28C3/06 , F28F9/22 , F28F2009/228
摘要： A system includes a quench system that may cool a syngas generated in a gasification chamber. The quench system includes a quench chamber, a dip tube that may direct the syngas from the gasification chamber into a quench liquid to cool the syngas to generate a cooled syngas, a draft tube disposed circumferentially about the dip tube and that may receive the cooled syngas in a first direction. A first passage is disposed between a first wall of the dip tube and a second wall of the draft tube. The system also includes a first baffle that may receive the cooled syngas from the first passage. The first baffle may split a flow of the cooled syngas into a first syngas flow and a second syngas flow, and the first baffle may redirect the first syngas flow in a second direction different from the first direction.
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公开(公告)号：US20180094199A1
公开(公告)日：2018-04-05
申请号：US15725637
申请日：2017-10-05
发明人： Douglas R. Bull , Ross M. Patten , Paul CAIRNEY , Gerald M. Cox , William P. Jepson , Benjamin F. Gardner
CPC分类号： C10J3/466 , B01J8/1809 , B01J8/1827 , B01J2208/00893 , B01J2208/00902 , C02F11/10 , C02F11/12 , C02F11/121 , C10J3/482 , C10J3/84 , C10J2300/0909 , C10J2300/0916 , C10J2300/0923 , C10J2300/0956 , C10J2300/1643 , C10J2300/1807 , C10K1/026 , Y02P20/129 , Y02W10/40 , Y10T29/49
摘要： A fluidized bed biogasifier is provided for gasifying biosolids. A feeder feeds biosolids into a reactor vessel at a desired feed rate during steady-state operation. A fluidized bed in the base of the reactor vessel has a cross-sectional area that is proportional to at least the fuel feed rate such that the superficial velocity of gas is in the range of 0.1 m/s to 3 m/s. The biosolids are heated inside the fluidized bed reactor to a temperature range between 900° F. and 1700° F. in an oxygen-starved environment having a sub stoichiometric oxygen level, whereby the biosolids are gasified. A burner system having a hooded nozzle below the fluidized bed in the reactor vessel provides high temperature gas to the biogasifier.
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47.发明申请公开(公告)号：US20180085761A1
公开(公告)日：2018-03-29
申请号：US15809318
申请日：2017-11-10
发明人： Horst Dressler , Michael Hofmeister
CPC分类号： B04C5/04 , B04C5/081 , C10B27/00 , C10B49/02 , C10B53/02 , C10J3/20 , C10J3/26 , C10J3/42 , C10J3/723 , C10J3/84 , C10J2200/152 , F23B80/00 , F23C5/32 , Y02E50/14
摘要： A cyclone separator for separating particles from a gas flow includes a gas inlet and a separating element. The separating element includes an upper cylindrical section connected to a gas outlet and a lower conical section connected to a particle outlet. The first end of the gas inlet is on a straight section, and the second end of the gas inlet in on a helical section. The second end is connected to the upper cylindrical section. The cross-sectional area of the gas inlet continually decreases, and the vertical or longitudinal dimension of the gas inlet continually increases from the first end towards the second end. The vertical dimension at the second end equals the diameter of the upper cylindrical section. A guide plate inside the straight section distributes the particles over the increasing vertical dimension of the gas inlet and prevents the particles from concentrating centrally in the gas flow.
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公开(公告)号：US09926502B2
公开(公告)日：2018-03-27
申请号：US15038792
申请日：2014-11-21
发明人： Wei Xin , Honghai Li , Ruiheng Gao , Yongjin Chen , Xiaofei Li , Pin Liu , Lizhi Li
CPC分类号： C10J3/84 , C01B3/02 , C10J3/485 , C10J3/845 , C10J2300/093 , C10J2300/0959 , C10J2300/1631 , C10J2300/1807 , C10J2300/1846
摘要： A carbonaceous substance powder gasification system and gasification method. The system comprises a carbonaceous substance reaction apparatus and a gas return apparatus used for raising the pressure of some of a raw syngas cooled and preliminarily purified downstream of the reaction apparatus, then blending with high-temperature raw syngas upstream of the reaction apparatus and reducing the temperature. The method comprises reacting in a gasification reaction apparatus the carbonaceous substance and a gasification agent to generate raw syngas and ash and slag, some of the high-temperature raw syngas moving downstream with fly ash and liquid slag, and some of the high-temperature syngas moving upstream with fly ash; the downstream part of the high-temperature raw syngas being cooled, preliminarily purified and deslagged, then pressurized, and the wet raw syngas being injected into the system and blended with the upstream high-temperature raw syngas; the remainder of the high-temperature syngas moving upstream with fly ash and blending and cooling with the low-temperature wet syngas injected by the preliminary cooler, and optionally being entered into the cooling reaction stage; the cooled or cooling-reacted raw syngas continuing upstream, passing through the upper cooling stage and cooling again and ash being removed to obtain the raw syngas.
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公开(公告)号：US09868916B1
公开(公告)日：2018-01-16
申请号：US14484867
申请日：2014-09-12
申请人： Yongchao Li
发明人： Yongchao Li
CPC分类号： C10J3/845 , C10J2300/1884
摘要： Methods, systems, and apparatus for cooling hot product gas are provided. The method includes introducing cooled solid into a downward or upward contactor where heat transfer between solid and product gas. After separating solid and product gas in cyclone system, cooled product gas flows to process downstream and hot solid is introduced into a fluidized bed solid cooler from the cyclone dipleg. The hot solid flows through the shell side of the fluidized bed cooler and exchanger heat with the coolant in the tube side. The cooled solid flows through a mechanical or non-mechanical valve back into the downward/upward contactor and complete the cycle.
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公开(公告)号：US20170369801A1
公开(公告)日：2017-12-28
申请号：US15204602
申请日：2016-07-07
申请人： Gaston GLOCK
发明人： Gaston GLOCK
CPC分类号： C10J3/84 , B01D46/2407 , B01D2273/20 , C10J3/26 , C10J3/721 , C10J2300/092 , C10J2300/0956 , C10K1/024 , C10K3/005 , Y02E20/16 , Y02E50/14
摘要： An apparatus and a method for gasifying carbon-containing materials in which the material for gasification and oxygen, usually in the form of air, are supplied to a gas generator where the gasification takes place in a fixed bed reactor. The product gas is drawn off via a product gas line and introduced into a hot gas filter. A filter, preferably provided with filter candles, removes solids such as particles not yet gasified, ash and foreign bodies, while clean gas passes through and is taken off via a clean gas line. An outlet is provided in the bottom region of the hot gas filter to remove residual solids. The hot gas filter is supplied through a line with oxygen, preferably in the form of air, in its middle height region, between the filter bottom and the outlet.
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