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公开(公告)号:US20230191317A1
公开(公告)日:2023-06-22
申请号:US17997736
申请日:2021-04-23
发明人: Ying Hui GUO
CPC分类号: B01D53/265 , B01D53/002 , B01D53/261 , B01D53/0446 , B01J20/3458 , B01D2253/102 , B01D2253/104 , B01D2253/116 , B01D2257/80 , B01D2257/102 , B01D2257/104 , B01D2259/402 , B01D2259/40001 , B01D2259/40088
摘要: An adsorptive separation apparatus comprises an upper air pipe, a lower air pipe, an adsorption pipe assembly located between the upper air pipe and the lower air pipe, an oil-water separation seat located at an end of the lower air pipe, and an oil-water separator arranged in the oil-water separation seat. An inner cavity is formed in the oil-water separation seat, and an air intake port is provided on the outer side surface of the oil-water separation seat. The inner cavity is in communication with the air intake port and the lower air pipe. The oil-water separator is located in the inner cavity. The oil-water separator comprises a separator housing and multiple layers of wire meshes filled inside the separator housing. Multiple through holes are formed on the separator housing.
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公开(公告)号:US20190184320A1
公开(公告)日:2019-06-20
申请号:US15842365
申请日:2017-12-14
申请人: FECC, INC.
发明人: Gordon Kirkland , Elgin Kirkland , Phil Lamori , Don Clift , Victor San Agustin
CPC分类号: B01D45/02 , B01D46/0027 , B01D46/4263 , B01D50/002 , B01D53/002 , B01D53/265 , B09C1/06 , E21B7/027 , G01N1/2205 , G01N2001/2282
摘要: An off-gas conditioning system includes a source of off-gas, at least one testing port, in communication with the source of off-gas wherein the testing port is connected to a meter capable of testing at least one metric selected from the group consisting of temperature, pressure, flow rate, and humidity. A first vapor-liquid separator in communication with and downstream of the source of off-gas, a second vapor liquid separator in communication with and downstream of the first vapor liquid separator, wherein at least one of the first or second vapor-liquid separators includes a heat-exchanger for cooling the off-gas, and wherein at least one of said first or second vapor liquid separators includes a particulate filter for removing particulates from the off-gas. at least one testing port, downstream of the second vapor-liquid separator in communication with at least one analyzer for analyzing said off-gas for specific chemical compounds.
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23.
公开(公告)号:US20190049191A1
公开(公告)日:2019-02-14
申请号:US15842515
申请日:2017-12-14
CPC分类号: F28D21/0001 , B01D1/0058 , B01D1/26 , B01D3/065 , B01D3/146 , B01D53/002 , B01D53/1456 , B01D53/263 , C02F1/16 , C02F2103/08 , C10G5/06 , C10G7/00 , F01K25/06 , F01K25/10 , F01K27/02 , F25J3/0209 , F25J3/0233 , F25J3/0238 , F25J3/0242 , F25J2200/02 , F25J2200/70 , F25J2200/74 , F25J2215/62 , F25J2240/70 , F25J2260/02 , F25J2270/12 , F25J2270/60 , F28D2021/0019
摘要: Certain aspects of natural gas liquid fractionation plant waste heat conversion to power using Kalina Cycle can be implemented as a system. The system includes a waste heat recovery heat exchanger configured to heat a buffer fluid stream by exchange with a heat source in a natural gas liquid fractionation plant. The system includes a Kalina cycle energy conversion system, which includes one or more first energy conversion heat exchangers configured to heat a working fluid by exchange with the heated buffer fluid stream, a separator configured to receive the heated working fluid and to output a vapor stream of the working fluid and the liquid stream of the working fluid, and a turbine and a generator, wherein the turbine and generator are configured to generate power by expansion of the vapor stream of the working fluid.
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公开(公告)号:US20190048753A1
公开(公告)日:2019-02-14
申请号:US15842160
申请日:2017-12-14
CPC分类号: F01K27/02 , B01D1/0058 , B01D1/0082 , B01D1/26 , B01D3/065 , B01D3/146 , B01D53/002 , B01D53/1456 , B01D53/263 , C02F1/16 , C02F2103/08 , C10G5/06 , C10G7/00 , F01K25/10 , F25B27/02 , F25J3/0209 , F25J3/0233 , F25J3/0238 , F25J3/0242 , F25J2240/60 , F25J2260/02 , F25J2270/12 , F25J2270/60 , F25J2270/902 , F28D21/0001 , F28D2021/0019
摘要: Certain aspects of natural gas liquid fractionation plant cooling capacity and potable water generation using integrated vapor compression-ejector cycle and modified multi-effect distillation system can be implemented as a system. The system includes a waste heat recovery heat exchanger network thermally coupled to multiple heat sources of a Natural Gas Liquid (NGL) fractionation plant. The heat exchanger network is configured to recover at least a portion of heat generated at the multiple heat sources. The system includes a first sub-system thermally coupled to the waste heat recovery heat exchanger to receive at least a first portion of heat recovered by the heat exchanger network. The first sub-system is configured to perform one or more operations using at least the first portion of heat recovered by the heat exchanger network.
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25.
公开(公告)号:US20190015773A1
公开(公告)日:2019-01-17
申请号:US15773213
申请日:2016-11-03
发明人: Tai Gyu LEE , Yu jin EOM , Woo Rim LEE
CPC分类号: B01D53/005 , B01D46/02 , B01D53/002 , B01D2257/602 , B09B3/00 , B09B3/0083 , B09B5/00 , B09C1/005 , B09C1/06
摘要: The present invention relates to an apparatus for treating waste containing mercury and a method for recovering high purity elemental mercury using the apparatus. More specifically, the present invention may provide a method that can more economically and stably recover high purity elemental mercury from waste containing mercury using an apparatus for recovering mercury from waste containing mercury, the apparatus comprising: a thermal desorption unit; a dust control unit; and a condensation and recovery unit, which are connected in series. The present invention has an advantage in that, compared to a conventional simple heat treatment-condensation method, a high recovery rate of mercury is achieved and high purity mercury can be obtained.
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公开(公告)号:US20180363979A1
公开(公告)日:2018-12-20
申请号:US16060674
申请日:2016-12-08
CPC分类号: F25J3/0242 , B01D3/06 , B01D3/148 , B01D5/00 , B01D5/006 , B01D53/002 , B01D53/229 , B01D53/24 , B01D2256/16 , B01D2256/24 , B01D2257/7022 , B01D2257/7025 , C10G5/06 , C10G31/06 , C10G70/00 , C10G2300/1081 , C10G2300/1088 , C10G2300/1092 , C10G2400/20 , F25J3/0209 , F25J3/0219 , F25J3/0233 , F25J3/0238 , F25J2200/02 , F25J2240/40 , Y02C20/20 , Y02P70/34
摘要: Selective recovery of C2 to C4 hydrocarbons is achieved through the use of a converging-diverging nozzle, or de Laval nozzle. The vapor stream comprising C2 to C4 hydrocarbons is fed into an inlet of a de Laval nozzle having a throat. The vapor stream may have an initial temperature of between 0° C. and 100° C., and an initial pressure of between 200 psig and 500 psig. In the de Laval nozzle, the vapor stream expands after passing through the throat of the de Laval nozzle, producing a vapor stream having reduced temperature and pressure. Then, C2 to C4 hydrocarbons condense from the reduced-temperature vapor stream as liquid droplets, which may be recovered. Fractionation of C2 to C4 hydrocarbons by means of a de Laval nozzle is possible; the technique allows selective recovery of a stream enriched in propene from a mixture of propane and propene.
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公开(公告)号:US20180354895A1
公开(公告)日:2018-12-13
申请号:US15573452
申请日:2016-12-21
申请人: Stamicarbon B.V.
发明人: Giusy Elisa PUCI , Joey DOBREE
IPC分类号: C07C273/04 , C07C273/16 , C01C1/18 , B01D53/00 , B01D53/14
CPC分类号: C07C273/04 , B01D53/002 , B01D53/1493 , B01D2251/404 , B01D2251/504 , B01D2252/10 , B01D2257/406 , C01C1/185 , C05C1/00 , C07C273/16 , C05C9/02
摘要: The invention relates to a process for the production of urea ammonium nitrate, a system and a method of modifying a plant. The process comprises subjecting ammonia-containing off-gas resulting from the production of ammonium nitrate (AN off-gas) to condensation under acidic conditions so as to form an acidic condensate, and using at least part of the acidic condensate as an acidic scrubbing liquid in a finishing treatment section having a gas inlet in fluid communication with a gas outlet of a finishing section of a urea production unit, wherein the finishing section is adapted to solidify urea liquid, and wherein said finishing treatment section is adapted to subject ammonia-containing off-gas of the finishing section to treatment with an acidic scrubbing liquid.
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公开(公告)号:US20180328660A1
公开(公告)日:2018-11-15
申请号:US15591882
申请日:2017-05-10
发明人: Nicole RUMORE
CPC分类号: F25J3/08 , B01D53/002 , B01D53/265 , F25J3/061 , F25J2220/02
摘要: Methods and systems for removing impurities (e.g. volatile organic compounds, water) from process gas streams, including condensing and freezing of the process gas stream, are provided herein.
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公开(公告)号:US20180299176A1
公开(公告)日:2018-10-18
申请号:US15485495
申请日:2017-04-12
申请人: Larry Baxter , Kyler Stitt , Aaron Sayre , Christopher Hoeger
发明人: Larry Baxter , Kyler Stitt , Aaron Sayre , Christopher Hoeger
CPC分类号: B01D7/02 , B01D1/0094 , B01D53/002 , B01D2256/245 , B01D2257/106 , B01D2257/302 , B01D2257/404 , B01D2257/602 , B01D2257/90 , B01D2257/93 , B01D2258/0283
摘要: A process to prevent fouling using a desublimating heat exchanger is disclosed. An outlet stream from the desublimating heat exchanger may be split into a plurality of parallel streams. The parallel streams may be sent through other devices for performing a unit operation, and the devices for performing a unit operation may change the temperature of at least one of the parallel streams. Parallel streams of differing temperature may emerge from the devices for performing a unit operation. The parallel streams of differing temperature may be sent to a mixing chamber. A mixed stream of uniform temperature may emerge from the mixing chamber, and the mixed stream may be recycled back to the desublimating heat exchanger. The mixing chamber may be separate from the desublimating heat exchanger, or the parallel streams of differing temperature may be mixed in the desublimating heat exchanger.
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公开(公告)号:US20180275024A1
公开(公告)日:2018-09-27
申请号:US15933353
申请日:2018-03-22
发明人: Stevie Horton Smith
CPC分类号: G01N1/2247 , B01D45/08 , B01D53/002 , B01D53/30 , B01D2257/70 , B01D2257/80 , C07C4/02 , G01N1/2035 , G01N1/2202 , G01N2001/2267 , G01N2001/2282 , C07C11/04 , C07C11/06
摘要: A distillation probe includes a conduit having a central axis. In addition, the distillation probe includes a baffle assembly disposed in the conduit. The baffle assembly includes a plurality of axially-spaced baffles positioned one-above-the-other in a stack within the conduit. Further, the distillation probe includes a first helical cooling coil wrapped around the conduit. Moreover, the distillation probe includes a thermally conductive layer disposed about the conduit and encapsulating the first helical cooling coil. The thermally conductive layer is configured to transfer thermal energy between the first helical cooling coil and the conduit.
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