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1.
公开(公告)号:US20240350962A1
公开(公告)日:2024-10-24
申请号:US18136990
申请日:2023-04-20
发明人: Andrea Leoncini , Zhijie Chua
CPC分类号: B01D53/002 , B01D8/00 , B01D53/75 , B01D2221/14 , B01D2257/108 , B01D2257/11 , B01D2258/0216
摘要: Chemical precursor recovery systems and methods of recovering and reusing semiconductor manufacturing chemistry are disclosed. The recovery systems include a cold trap inlet line in fluid communication with a plurality of cold traps and a cold trap outlet line. The plurality of cold traps is configured to condense the chemical precursors and are arranged based on semiconductor manufacturing process conditions.
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公开(公告)号:US20240343578A1
公开(公告)日:2024-10-17
申请号:US18606018
申请日:2024-03-15
IPC分类号: C01B23/00 , B01D53/00 , B01D53/047 , B01D53/14 , B01D53/22 , B01D53/26 , B01D53/46 , C01B32/50 , F25J3/02
CPC分类号: C01B23/0094 , B01D53/002 , B01D53/047 , B01D53/1475 , B01D53/229 , B01D53/26 , B01D53/46 , C01B32/50 , F25J3/029 , B01D2251/102 , B01D2252/20431 , B01D2252/20447 , B01D2252/20489 , B01D2256/18 , B01D2257/102 , B01D2257/108 , B01D2257/504 , B01D2257/702 , B01D2257/80 , C01B2210/0004 , C01B2210/001 , C01B2210/0014 , C01B2210/0025 , C01B2210/0031 , C01B2210/0046 , C01B2210/0051 , C01B2210/0053 , C01B2210/0062 , C01B2210/007 , F25J2205/30 , F25J2205/40 , F25J2205/64 , F25J2205/80 , F25J2205/82 , F25J2210/20 , F25J2215/30 , F25J2220/02 , F25J2240/40 , F25J2270/30 , F25J2270/42 , F25J2270/58
摘要: The present provides a helium gas separation and recovery process involving cryogenic fractionation process, which comprises cooling a dehydrated high-pressure gas stream while maintain velocity and pressure of the stream; reducing pressure of the dehydrated high-pressure gas stream via a Joule-Thompson's process to obtain a partially liquefied gas stream; and iii) subjecting the partially liquefied gas stream to at least one gas-liquid separation process to obtain at least one liquid stream and a gaseous stream comprising helium, and a residual amount of the gaseous components; recycling the liquid stream obtained in step iii) for use as cooling refrigerant to cool the dehydrated high-pressure gas stream; and purifying the unrefined helium gas stream using pressure swing adsorption (PSA) and/or membrane separation process to obtain a helium product stream having a purity of 98.0 mole % or more.
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公开(公告)号:US20240342651A1
公开(公告)日:2024-10-17
申请号:US18747932
申请日:2024-06-19
IPC分类号: B01D53/78 , B01D47/05 , B01D47/10 , B01D53/00 , B01D53/75 , B03C3/017 , B03C3/04 , B03C3/16 , B03C5/02 , B03C7/02 , B03C11/00 , F23G7/06 , F23J15/00 , F23J15/02
CPC分类号: B01D53/78 , B01D53/002 , B01D53/75 , B03C3/017 , B03C3/04 , B03C3/16 , B03C5/02 , B03C7/02 , B03C11/00 , F23G7/06 , F23J15/006 , F23J15/022 , B01D47/05 , B01D47/10 , B01D2247/10 , B01D2251/106 , B01D2251/108 , B01D2257/304 , B01D2257/406 , B01D2257/70 , B01D2257/708 , B01D2257/80 , B01D2257/90 , B01D2257/93 , F23J2217/102 , F23J2219/40 , F23J2219/70
摘要: A method for removing noxious, hazardous, toxic, mutagenic, and/or carcinogenic compounds and/or precursor compounds from a comingled gas, liquid, and/or solid stream is described. In one embodiment, the method is used to prepare the stream for feeding to an oxidizer, such as a thermal oxidizer, to reduce the amount of particulate matter discharged by the oxidizer and includes passing the stream through an ambient or chilled temperature condenser followed by an optional gas/solid separator, and one or more gas scrubbers prior to feeding to the oxidizer.
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公开(公告)号:US20240335783A1
公开(公告)日:2024-10-10
申请号:US18587403
申请日:2024-02-26
发明人: Yongchen SONG , Lanlan JIANG , Mingjun YANG , Bingbing CHEN , Yu LIU , Jing CHEN
CPC分类号: B01D53/002 , B01D53/62
摘要: The present invention belongs to the application field of hydrate technology, and discloses a large-scale integrated device of CO2 capture, sequestration and utilization and method. The device separates and purifies CO2 in a forward or reverse way; at the same time, it is configured with a storage simulation system to store the purified CO2; the system is configured with an axial pressure and circumferential pressure system, which can simulate the pressure environment of the deep-sea ocean and provide experimental support for the storage of CO2 in the deep-sea; and the device is reserved for the interface of seawater desalination system module, which can provide an experimental environment for the desalination of seawater by the hydrate method. Finally, the device is equipped with a cold storage system to realize the secondary utilization of energy from industrial high temperature exhaust gas.
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公开(公告)号:US12097461B2
公开(公告)日:2024-09-24
申请号:US17546786
申请日:2021-12-09
发明人: Guoqiang Chen , Senlin Tian , Ping Ning , Xiaosong Yang , Linan Shao , Zhilong Zhao
CPC分类号: B01D53/002 , B01D5/0021 , B01D5/0072 , B01D46/02
摘要: A method for treating arsenic-containing flue gas is disclosed. In the method, the arsenic-containing flue gas is subjected to a dry pre-dedusting treatment, and the dedusted flue gas is pre-cooled and then introduced into a vortex quenching system. The arsenic-containing flue gas is divided into high-temperature flue gas and low-temperature flue gas through the vortex quenching system. The outlet temperature of the low-temperature flue gas is dropped below the desublimation temperature of gaseous arsenic trioxide. The low-temperature flue gas is subjected to a gas-solid separation to obtain solid arsenic trioxide and treated flue gas.
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公开(公告)号:US12083541B2
公开(公告)日:2024-09-10
申请号:US17602487
申请日:2020-04-09
申请人: TWISTER B.V.
CPC分类号: B04C3/06 , B01D45/16 , B01D53/002 , B01D53/24 , B04C2003/003 , B04C2003/006
摘要: Provided is a cyclonic fluid separator, method of fluid separation, and a method of installing a cyclonic fluid separator. The cyclonic fluid separator includes a throat portion arranged between a converging fluid inlet section and a diverging fluid outlet section including an inner primary outlet for condensables depleted fluid components and an outer secondary outlet for condensables enriched fluid components. A central body extends along a central axis of the cyclonic fluid separator through at least part of the inlet section of the separator. The central body has, at a location upstream of the throat portion, a larger outer width than a smallest inner width of the throat portion; swirl imparting means arranged in the inlet section for creating a swirling motion of the fluid within at least part of the separator. The swirl imparting means are adjustable; and an adjusting mechanism configured for adjusting the swirl imparting means for varying the swirling motion of the fluid.
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公开(公告)号:US20240252978A1
公开(公告)日:2024-08-01
申请号:US18423547
申请日:2024-01-26
发明人: Larry Baxter
CPC分类号: B01D53/145 , B01D3/40 , B01D53/002 , B01D53/1406 , B01D53/1475 , B01D53/1493 , B01D53/18 , B01D53/263 , B01D53/265 , B01D2252/102 , B01D2252/2021 , B01D2252/204 , B01D2257/504 , B01D2257/80
摘要: A system and method separate a process fluid stream into a liquid-phase carbon dioxide stream and a carbon dioxide-depleted stream containing the remaining light gases. The system and method use a drying heat exchanger to contact the process fluid stream with a dryer contact liquid to remove moisture from a process fluid stream. The gaseous process fluid stream is separated from the wet dryer contact liquid stream and is directed to an extraction heat exchanger where it is contacted with an extraction contact liquid so that carbon dioxide is removed from the process fluid stream with a treated process fluid stream and a carbon dioxide enriched extraction contact liquid stream being formed.
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公开(公告)号:US20240208813A1
公开(公告)日:2024-06-27
申请号:US18086926
申请日:2022-12-22
CPC分类号: C01B3/506 , B01D53/002 , B01D53/047 , C01B3/047 , C01B3/56 , F01K25/08 , F25J3/062 , F25J3/0655 , F25J3/066 , C01B2203/042 , C01B2203/046 , C01B2203/0465 , C01B2203/84
摘要: A method for separating hydrogen and nitrogen from a gas mixture, including a) thereby partially condensing a hydrogen and nitrogen gas mixture and producing a two-phase stream, b) phase separating the two-phase stream, producing a nitrogen-enriched liquid fraction and a hydrogen-enriched gaseous fraction, c) expanding the nitrogen-enriched liquid fraction, producing a lower-pressure nitrogen-enriched liquid or two-phase stream, d) adding heat to the lower-pressure nitrogen-enriched liquid stream, producing a warm nitrogen enriched gaseous stream, and e) adding heat to the hydrogen-enriched gaseous fraction, producing a hydrogen-rich product stream. Wherein, at least a portion of the heat added in step d) is removed in step a), at least a portion of the heat added in step e) is removed in step a), or at least a portion of the heat added in step d) and at least a portion of the heat added in step e) is removed in step a).
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9.
公开(公告)号:US20240207772A1
公开(公告)日:2024-06-27
申请号:US18538251
申请日:2023-12-13
CPC分类号: B01D53/002 , B01D45/04 , B01D53/265 , B01D2257/404 , B01D2257/504 , B01D2257/80
摘要: A method is disclosed. The method includes directing a stream into a compressor station, the stream being a pre-cooled effluent gaseous stream including N2, O2, CO2, water vapor, and hazardous emissions when it is directed into the compressor station, bringing the stream to a medium range pressure by performing an isothermal compression using the compressor station, sending the stream into a first regenerative heat exchanger, at which a temperature of the stream is lowered to below a condensation temperature of CO2 by the purified cold stream after its expansion in the downstream expander and causing partial stream liquefaction thereby transitioning or transforming the incoming stream into a two-phase stream, directing the two-phase flow into one or more inertia separators to collect said liquid phase including liquefied emissions and CO2 in a pressurized storage, and directing a thusly purified gaseous portion of a two-phase stream that leaves the one or more inertia separators into an expander.
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公开(公告)号:US20240109002A1
公开(公告)日:2024-04-04
申请号:US17960128
申请日:2022-10-04
CPC分类号: B01D5/0054 , B01D5/0081 , B01D53/002
摘要: Embodiments presented provide a compressed air and liquid separator having a shell adapted to be vertically or horizontally oriented in use. The shell has an inlet end and an outlet end and defines a separating chamber therein. An inlet plate is coupled to the inlet end of the shell and provides a compressed gas ingress into the separating chamber, the compressed gas including a liquid therein. A plurality of inlet nozzles is disposed in the inlet plate, each inlet nozzle having an inner diameter and a length that are selected so as to accelerate the compressed gas therethrough to below a dew point thereof. A plurality of separating baffles positioned within the separating chamber above the compressed gas ingress, the separating baffles providing a means for separating the liquid from the compressed gas. An outlet plate is coupled to the outlet end of the shell, the outlet plate providing a compressed gas egress out of the separating chamber.
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