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公开(公告)号:US20240308852A1
公开(公告)日:2024-09-19
申请号:US18678425
申请日:2024-05-30
发明人: Suguru NODA , Katsuya NAMIKI , Zihao ZHANG , Toshio OSAWA , Hisashi SUGIME
IPC分类号: C01B32/162 , B01J4/00 , B01J6/00 , B82Y40/00
CPC分类号: C01B32/162 , B01J4/002 , B01J4/008 , B01J6/008 , B01J2204/002 , B82Y40/00
摘要: Provided are a carbon nanotube production device and production method capable of realizing high-temperature heating of a catalyst raw material in a floating catalyst chemical vapor deposition (FCCVD) method, and improving the quality and yield of carbon nanotubes synthesized. A carbon nanotube production device 1 includes a synthesis furnace 2 for synthesizing carbon nanotubes; a catalyst raw material supplying nozzle 3 for supplying a catalyst raw material used to synthesize carbon nanotubes to the synthesis furnace 2; and a nozzle temperature adjusting unit 6 capable of setting a temperature of an inner portion 4 of the catalyst raw material supplying nozzle 3 higher than a temperature of a reaction field 5 of the synthesis furnace 2. By supplying to the synthesis furnace 2 the catalyst raw material that has been thermally decomposed after being heated to a temperate at which a catalyst metal will not yet be condensed, and by having the thermally decomposed catalyst raw material rapidly cooled to a CVD temperature at the synthesis furnace 2, microscopic catalyst metal particles will be generated at a high density in the space of the reaction field 5 such that carbon nanotubes having a small diameter can be vapor-grown at a high density.
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公开(公告)号:US20240307842A1
公开(公告)日:2024-09-19
申请号:US18576009
申请日:2022-07-20
发明人: Yee Fun LIM , Yang XU , Jian Wei Jayce CHENG , Swee Liang WONG , Vijila CHELLAPPAN , Jatin KUMAR , Daniil BASH , Tonio BUONASSISI , Kedar HIPPALGAONKAR
IPC分类号: B01J19/00 , B01J4/00 , B01J14/00 , B01J19/24 , B29C64/314 , B29C64/393 , B33Y40/00 , B33Y50/02
CPC分类号: B01J19/0033 , B01J4/008 , B01J14/00 , B01J19/24 , B29C64/314 , B29C64/393 , B33Y40/00 , B33Y50/02 , B01J2204/002 , B01J2219/00164 , B01J2219/00202 , B01J2219/00243
摘要: The present disclosure generally relates to a flow reactor system (100) and a flow reaction method (200). The flow reactor system (100) comprises liquid pumps (110) for communicating liquid reagents based on a set of flow conditions, a fluid pump (200) for communicating a carrier fluid that is immiscible with the liquid reagents; a fluidic mixer (130) for mixing the liquid reagents into a liquid mixture, a measurement device (150) for measuring properties of liquid plugs (140) discharged from an outlet (136) of the fluidic mixer (130); and a control module configured for controlling the liquid pumps (110) and adjusting the flow conditions based on the measured properties of the liquid plugs (140), wherein the liquid plugs (140) are representative of different flow conditions.
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公开(公告)号:US12076712B2
公开(公告)日:2024-09-03
申请号:US17431902
申请日:2020-02-24
CPC分类号: B01J3/008 , B01J4/008 , C02F11/086 , C02F2201/005 , C02F2209/02 , C02F2209/03 , C02F2301/066
摘要: Aqueous effluent treatment system including a separation reactor having a reactor chamber fluidly connected to an aqueous effluent source, connected via a pump to an inlet of the reactor chamber, a fluid extraction system connected to a liquid effluent outlet at a top of the reactor chamber, and a solid residue extraction system connected to a solid residue outlet at a bottom of the reactor chamber. The separation reactor is operable to generate pressures exceeding 22 MPa and temperatures exceeding 300° C. in the reactor chamber configured to generate a supercritical zone in an upper portion of the reactor chamber to which the liquid effluent outlet is connected, and a subcritical zone in a lower portion of the chamber within the reactor chamber to which the solid residue outlet is connected. The solid residue extraction system comprises an output circuit comprising a collector coupled to the solid residue outlet via a collector input valve (V1) and to a water output tank via a filter and a collector liquid output valve (V4) operable to be opened to cause a pressure drop at the solid residue outlet to draw solid residue out of the reactor chamber, the solid residue extraction system further comprising a gas feed circuit connected via a gas supply valve (V5) to the collector, the gas supply valve operable to be opened to extract solid residues in the collector to a solids output tank connected to the collector via a collector solids output valve (V6).
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公开(公告)号:US12065398B2
公开(公告)日:2024-08-20
申请号:US17310074
申请日:2020-01-14
发明人: Joseph William Schroer , Scott Stevenson , Andrew Mark Ward , Tim Abbott , Kenneth Francis Lawson , Michael Edward Huckman , Zhun Zhao , Arno Oprins
IPC分类号: C07C29/152 , B01D53/047 , B01D53/26 , B01J4/00 , B01J6/00 , B01J19/00 , B01J19/24 , C01B3/12 , C01B3/34 , C01B3/48 , C01B3/56 , C01C1/02 , C01C1/04 , C07C4/02 , C07C4/04 , C07C29/132 , F25J3/02 , H01M8/04082 , H01M8/0606 , H01M8/0612 , H02J15/00 , H01M8/1007
CPC分类号: C07C29/152 , B01D53/047 , B01D53/265 , B01J4/008 , B01J6/008 , B01J19/0033 , B01J19/0053 , B01J19/2465 , C01B3/12 , C01B3/342 , C01B3/48 , C01B3/56 , C01C1/02 , C01C1/0417 , C01C1/0488 , C07C4/02 , C07C4/04 , C07C29/132 , F25J3/0233 , H01M8/04201 , H01M8/0606 , H01M8/0618 , H02J15/006 , H02J15/008 , B01D2256/16 , B01D2256/245 , B01J2219/00051 , B01J2219/00132 , B01J2219/00761 , B01J2219/0871 , C01B2203/0216 , C01B2203/0233 , C01B2203/0238 , C01B2203/0244 , C01B2203/0261 , C01B2203/0283 , C01B2203/0294 , C01B2203/04 , C01B2203/061 , C01B2203/066 , C01B2203/068 , C01B2203/085 , C01B2203/148 , H01M8/1007
摘要: A methanol synthesis plant comprising: a feed pretreating section operable to pretreat a feed stream; a synthesis gas (syngas) generation section comprising one or more reactors operable to produce a syngas synthesis product stream comprising synthesis gas from the feed stream; a methanol synthesis section comprising one or more methanol synthesis reactors operable to produce a synthesis product comprising methanol; and/or a methanol purification section operable to remove at least one component from the synthesis product to provide a purified methanol product; wherein the methanol synthesis plant is configured such that, relative to a conventional methanol synthesis plant, more of the net energy required by the methanol synthesis plant, the feed pretreating section, the syngas generation section, the methanol synthesis section, the methanol purification section, or a combination thereof, is provided by a non-carbon based energy source, a renewable energy source, and/or electricity.
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公开(公告)号:US20240270586A1
公开(公告)日:2024-08-15
申请号:US18535938
申请日:2023-12-11
发明人: Wenbiao ZHANG , Chaocai PENG , Guoliang JIA , Lei WANG , Chao TANG , Longlin SUN , Linlin WU
CPC分类号: C01C1/04 , B01J4/008 , B01J8/02 , B01J19/0033 , B01J19/088 , F17C7/00 , B01J2208/00752 , B01J2219/00164 , F17C2201/0128 , F17C2201/032 , F17C2221/012 , F17C2227/0157 , F17C2250/03
摘要: An ammonia synthesis system and a control method thereof are provided. The ammonia synthesis system includes a hydrogen supply device, where a fluctuating amount of hydrogen is provided by the hydrogen supply device; a hydrogen storage container configured to store the hydrogen provided by the hydrogen supply device; and a nitrogen supply device configured to communicate with the hydrogen storage container to introduce nitrogen into the hydrogen storage container to maintain a stable pressure in the hydrogen storage container. The nitrogen supply device is able to introduce nitrogen into the hydrogen storage container, thus the amount of hydrogen provided is stable; in addition, the ammonia synthesis system can not only meet requirements of application scenarios where synthesis gas is produced from conventional raw material, but also be well applied to application scenarios where hydrogen for ammonia synthesis is obtained from hydrogen generation by green electricity.
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公开(公告)号:US12018213B2
公开(公告)日:2024-06-25
申请号:US17773796
申请日:2020-11-03
发明人: Marvine Besong , Colin Kedge
IPC分类号: C10B53/07 , B01J4/00 , B01J6/00 , B65G33/22 , B65G33/24 , C10B3/02 , C10B7/10 , C10B49/22 , C10G1/10 , F23G5/30
CPC分类号: C10B7/10 , B01J4/007 , B01J4/008 , B01J6/008 , B65G33/22 , B65G33/24 , C10B3/02 , C10B49/22 , C10B53/07 , C10G1/10 , F23G5/30 , B01J2204/002 , B01J2204/007 , C10G2300/1003 , F23G2201/00 , F23G2205/121 , F23G2207/20 , F23G2209/28
摘要: A feed system for a reactor, a reactor assembly comprising such a feed system, and a method of supplying a feed material to a reactor with a feed system are provided. The reactor may be a pyrolysis reactor, such as a fluidised bed pyrolysis reactor. A method of pyrolysing a feed material is also provided. The feed system may comprise a feed conduit extending from an inlet to an outlet, and may have a first section including the inlet and a second section including the outlet. The first section may accommodate an auger. The second section may comprise at least one plug forming zone in which feed material is compressed into a substantially gas-tight plug during operation. There may be a temperature regulator for controlling the temperature in the second section. The temperature regulator may comprise a cooling jacket.
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公开(公告)号:US20240101511A1
公开(公告)日:2024-03-28
申请号:US18532040
申请日:2023-12-07
发明人: Todd COLEMAN , Tim YEAMAN , Slaton FRY
IPC分类号: C07C407/00 , B01J4/00 , B01J8/00 , B01J8/02
CPC分类号: C07C407/00 , B01J4/008 , B01J8/001 , B01J8/0278 , B01J2204/005 , B01J2208/00628 , B01J2208/00823 , B01J2208/00964
摘要: A method of producing an organic peroxide includes introducing an organic solution and a peroxide solution into a mixing tank to form a mixture. The method further includes circulating the mixture over a fixed catalyst bed to form the organic peroxide and measuring a concentration of the organic peroxide in the mixture. Further, the method includes removing at least a portion of the mixture when the concentration reaches a set value.
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公开(公告)号:US11938473B2
公开(公告)日:2024-03-26
申请号:US16646940
申请日:2017-11-14
申请人: ONEJOON GMBH
CPC分类号: B01J6/004 , B01J4/002 , B01J4/008 , F27B2007/365 , F27B9/028 , F27B9/2407 , F27B2009/3638 , F27B9/40
摘要: The invention relates to a device for the thermal or thermo-chemical treatment, more particularly calcination, of material (12), more particularly battery cathode material (14), comprising a housing (16), in which a process space (20) is located. The material (12), or carrying structures (40) loaded with the material (12), can be conveyed in a conveying direction (30) into or through the process space (20) by means of a conveying system (28). A process space atmosphere (50) prevailing in the process space (20) can be heated by means of a heating system (48). There is a process gas system (64), by means of which a process gas (66) can be fed to the process space (20), said process gas being required for the thermal treatment of the material (12). The process gas system (64) comprises a plurality of local injection units (68), which are arranged and configured such that process gas (66) can be released in a targeted manner onto the material (12) or onto the carrying structures (40) loaded with material (12), the process gas being released in a plurality of local process gas streams (70), each having a main stream direction (72). The invention also specifies a method for the thermal or thermo-chemical treatment of material (12), in which process gas (66) is released in a targeted manner onto the material (12) or onto the carrying structures (40) loaded with material (12), the process gas being released in a plurality of local process gas streams (70), each having a main stream direction (72).
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公开(公告)号:US20240084203A1
公开(公告)日:2024-03-14
申请号:US18263888
申请日:2022-01-27
发明人: Zhenwei WANG , Liqing YANG , Bairen ZHAO , Mingrui ZHAO , Gang LIU
CPC分类号: C10G9/002 , B01D3/007 , B01D3/141 , B01J4/008 , B01J19/0013 , C10G5/06 , C10G7/00 , B01J2204/007 , B01J2219/00103 , C10G2400/02
摘要: A heat recovery apparatus and process for cracked gas are provided. The cracked gas comprises liquid feedstock cracked gas and gaseous feedstock cracked gas, and the apparatus comprises a heat recovery device for liquid feedstock cracked gas, a heat recovery device for gaseous feedstock cracked gas and a heavy component removal unit. The invention solves the problems in the art, i.e., incomplete heat recovery technology for cracked gas, insufficient control of viscosity of quench oil, high capital investment and large footprint of the equipment, as well as unstable operation and high energy consumption.
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公开(公告)号:US11873273B2
公开(公告)日:2024-01-16
申请号:US16981666
申请日:2019-03-28
发明人: Todd Coleman , Tim Yeaman , Slaton Fry
IPC分类号: C07C407/00 , B01J4/00 , B01J8/00 , B01J8/02
CPC分类号: C07C407/00 , B01J4/008 , B01J8/001 , B01J8/0278 , B01J2204/005 , B01J2208/00628 , B01J2208/00823 , B01J2208/00964
摘要: A method of producing an organic peroxide includes introducing an organic solution and a peroxide solution into a mixing tank to form a mixture. The method further includes circulating the mixture over a fixed catalyst bed to form the organic peroxide and measuring a concentration of the organic peroxide in the mixture. Further, the method includes removing at least a portion of the mixture when the concentration reaches a set value.
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