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61.发明授权
公开(公告)号：US4073628A
公开(公告)日：1978-02-14
申请号：US746245
申请日：1976-12-01
CPC分类号： C10J3/723 , C10J3/50 , C10J3/57 , C10J3/78 , C10J2300/093 , C10J2300/0959 , C10J2300/0976 , Y10S48/02 , Y10S48/04
摘要： Fine-grain fuel is delivered from pressure vessels with a vehicle gas as a fluidized flow into a reactor for gasification at an elevated pressure. A gaseous gasification agent is also fed into the reactor. A control system for the fine-grain fuel and gasification agent includes detectors to provide an electrical signal which varies during feeding of fuel from the pressure vessels into the reactor. Controllers produce a fuel rate control signal corresponding to a comparison between the electrical signal from the detectors and a predetermined reference value corresponding to the desired fuel supply rate. Control valves respond to the fuel rate control signal to adjust the supply of vehicle gas to transfer fuel from the pressure vessels into the reactor. When a plurality of pressure vessels is used, then separate detectors, controllers and control valves form part of a control system which further includes computing means to provide a summation signal corresponding to the output signals from the various detectors. The summation signal is used by the various controllers for adjusting the control valves associated with each pressure vessel. A further controller produces a gasification agent control signal in response to a comparison between the summation signal and a predetermined reference value corresponding to a desired supply rate of gasification agent into the reactor. A control valve is operated in response to the gasification agent control signal. The control system further includes a gas analyzer responsive to the gaseous product from the reactor to monitor the supply of gasification agent into the reactor and adjust the supply thereof to the reactor.
摘要翻译： 细粒燃料从压力容器输送，车辆气体作为流化流进入反应器，以在升高的压力下气化。 还将气态气化剂进料到反应器中。 用于细粒燃料和气化剂的控制系统包括检测器，用于提供在从压力容器进入反应器的燃料供给期间变化的电信号。 控制器产生对应于来自检测器的电信号与对应于期望燃料供应速率的预定参考值之间的比较的燃料速率控制信号。 控制阀响应于燃料速率控制信号以调节车辆气体的供应以将燃料从压力容器传送到反应器中。 当使用多个压力容器时，分离的检测器，控制器和控制阀构成控制系统的一部分，该控制系统还包括计算装置，以提供对应于来自各种检测器的输出信号的求和信号。 求和信号由各种控制器用于调节与每个压力容器相关联的控制阀。 响应于加和信号与对应于进入反应器的气化剂的期望供应速率的预定参考值之间的比较，另一个控制器产生气化剂控制信号。 响应于气化剂控制信号操作控制阀。 控制系统还包括气体分析仪，其响应来自反应器的气态产物，以监测气化剂供应到反应器中并调节其供应到反应器。
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公开(公告)号：US3775071A
公开(公告)日：1973-11-27
申请号：US3775071D
申请日：1971-07-20
CPC分类号： C10J3/482 , B01J3/02 , C10G1/06 , C10J3/30 , C10J2300/0966 , C10J2300/1659 , C10J2300/1807
摘要： A method for continuous feeding of dry coal particles from essentially atmospheric pressure to the superatmospheric pressure level of a coal gasifier or coal liquefaction reactor is achieved by a series of screw feeding devices each partially boosting the pressure level of the coal in stages to provide the dry coal at reactor pressure.
摘要翻译： 通过一系列螺旋进料装置实现将干煤颗粒从基本上大气压连续进料到超大气压力水平的方法，每个螺杆进料装置分别部分地提高煤的压力水平以提供干燥 煤在反应堆压力。
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63.发明授权Process for supplying plasticizable carbonaceous solids into a gasification zone 失效将可塑性碳质固体供应到气化区的方法
公开(公告)号：US2577632A
公开(公告)日：1951-12-04
申请号：US69329846
申请日：1946-08-27
申请人： STANDARD OIL DEV CO
发明人： ROETHELI BRUNO E
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公开(公告)号：US11802251B2
公开(公告)日：2023-10-31
申请号：US17651185
申请日：2022-02-15
CPC分类号： 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
摘要： 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.
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65.发明公开公开(公告)号：US20230287285A1
公开(公告)日：2023-09-14
申请号：US18139447
申请日：2023-04-26
申请人： Frichs Holding 2 ApS
发明人： Ove KUDAHL MUNCH
CPC分类号： C10J3/485 , C10J3/466 , C10J3/506 , C10J3/74 , C10J3/526 , C10J2300/092 , C10J2300/1246 , C10J2300/1823 , C10J2300/1884 , C10J2200/152 , C10J2200/158 , C10J2200/09
摘要： 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.
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公开(公告)号：US20220169933A1
公开(公告)日：2022-06-02
申请号：US17651185
申请日：2022-02-15
摘要： 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.
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公开(公告)号：US11193073B2
公开(公告)日：2021-12-07
申请号：US16746484
申请日：2020-01-17
发明人： Alex Wormser , John Parkes , Douglas M. Todd
摘要： A carbonaceous fuel gasification system for a supercritical CO2 power cycle system includes a micronized char preparation system comprising a devolatilizer that receives solid carbonaceous fuel, hydrogen, oxygen, and fluidizing steam and produces micronized char, steam, hydrogen, and volatiles. An indirect gasifier includes a vessel comprising a gasification chamber that receives the micronized char, a conveying gas, and steam where the gasification chamber provides syngas, ash, and steam. A combustion chamber receives syngas and an oxidant and burns the mixture of syngas with the oxidant to provide heat for gasification and for heating incoming flows, thereby generating steam and CO2. The heat for gasification is transferred from the combustion chamber to the gasification chamber by circulating refractory sand. A syngas cooler cools the syngas and generates steam and provides to a supercritical CO2 power cycle system that performs a supercritical CO2 power cycle for generating power.
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公开(公告)号：US10717594B2
公开(公告)日：2020-07-21
申请号：US16072286
申请日：2017-02-06
摘要： Provided is a pressurizing system which includes: a pressurizing nozzle configured to supply a pressurizing gas into a hopper (3) where pulverized coal is accumulated; a filter configured to face a space in the hopper (3) where the pulverized coal is accumulated, and to allow the pressurizing gas to pass through the filter, the filter being provided at an end of the pressurizing nozzle; buffer tanks (5a), (5b) in which a pressurizing gas to be supplied to the hopper (3) is collected at a first predetermined pressure; and a pressure control means configured to start, at a time of starting pressurization of the hopper (3), supply of a pressurizing gas at a second predetermined pressure which is lower than the first predetermined pressure of the pressurizing gas collected in the buffer tanks (5a), (5b).
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69.发明授权公开(公告)号：US10669494B2
公开(公告)日：2020-06-02
申请号：US16098208
申请日：2017-06-09
摘要： A system is disclosed provided with: a slag bath that retains slag cooling water and receives slag; a slag cooling water feed line and a slag pump outlet via which the slag and the slag cooling water are pumped and fed to a slag separation device; a circulation pump that forms a water flow for pumping out the slag; a slag cooling water circulation line linking from the slag separation device to the slag bath; a reverse flow line that causes the slag cooling water dispensed from the circulation pump to flow in reverse in the slag cooling water feed line; a selective supply unit capable of selectively supplying the slag cooling water dispensed from the circulation pump to the slag cooling water circulation line and the reverse flow line; and a water supply line, one end of which is connected to the slag cooling water feed line.
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70.发明申请公开(公告)号：US20200095898A1
公开(公告)日：2020-03-26
申请号：US16137721
申请日：2018-09-21
IPC分类号： F01K23/10 , F02C3/20 , F23C10/01 , F23C10/04 , F23C13/08 , F23C10/22 , F23R3/40 , C01B3/02 , C10J3/82 , C10J3/50
摘要： A chemical looping combustion (CLC) based power generation, particularly using liquid fuel, ensures substantially complete fuel combustion and provides electrical efficiency without exposing metal oxide based oxygen carrier to high temperature redox process. An integrated fuel gasification (reforming)-CLC-followed by power generation model is provided involving (i) a gasification island, (ii) CLC island, (iii) heat recovery unit, and (iv) power generation system. To improve electrical efficiency, a fraction of the gasified fuel may be directly fed, or bypass the CLC, to a combustor upstream of one or more gas turbines. This splitting approach ensures higher temperature (efficiency) in the gas turbine inlet. The inert mass ratio, air flow rate to the oxidation reactor, and pressure of the system may be tailored to affect the performance of the integrated CLC system and process.
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