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公开(公告)号:US20240198273A1
公开(公告)日:2024-06-20
申请号:US18079505
申请日:2022-12-12
发明人: Sagheer A. ONAIZI
CPC分类号: B01D53/025 , B01D53/0454 , B01D53/12 , B01J20/226 , B01J20/28007 , B01J20/28066 , B01J20/28073 , B01J20/2808 , B01J20/3085 , B01D2253/204 , B01D2253/304 , B01D2253/306 , B01D2253/308 , B01D2256/10 , B01D2256/245 , B01D2257/304 , B01D2259/126 , B01J2220/46
摘要: A process for removing hydrogen sulfide (H2S) from a H2S-containing gas composition includes charging a liquid to a reactor under continuous agitation and dispersing particles of a cobalt-based zeolitic imidazolate framework-67 (ZIF-67) in the liquid to form a ZIF-67 mixture. The method further includes introducing the H2S-containing gas composition to the reactor containing the ZIF-67 mixture under continuous agitation and passing the H2S-containing gas composition through the ZIF-67 mixture. In addition, the method includes adsorbing the H2S from the H2S-containing gas composition onto the ZIF-67 to remove the H2S from the H2S-containing gas composition and form a purified gas composition.
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2.
公开(公告)号:US20230330589A1
公开(公告)日:2023-10-19
申请号:US18042838
申请日:2021-08-10
申请人: SINTEF TTO AS
IPC分类号: B01D53/12
CPC分类号: B01D53/12 , B01D2258/0283 , B01D2257/504 , B01D2259/4009
摘要: Disclosed herein is a gas capture system comprising: a first reactor system arranged so that, in the first reactor system, at least some gas in a gas stream that is received by the gas capture system is captured by a sorbent that is arranged to flow through the first reactor system; a second reactor system arranged to regenerate the sorbent so that the sorbent releases at least some of the gas captured in the first reactor system, wherein the sorbent is arranged to flow through the second reactor system and the second reactor system is arranged to output a flow of the released gas; a first sorbent transfer system arranged between a sorbent outlet of the first reactor system and a sorbent inlet of the second reactor system, wherein the first sorbent transfer system comprises a lock hopper; and a second sorbent transfer system arranged between a sorbent outlet of the second reactor system and a sorbent inlet of the first reactor system, wherein the second sorbent transfer system comprises a lock hopper; wherein: the sorbent is a solid; the second reactor system comprises a pump arranged so that the second reactor system may have a lower operational pressure when regenerating sorbent than the operational pressure of the first reactor system during gas capture by the sorbent; and the first reactor system, first sorbent transfer system, second reactor system and second sorbent transfer system are all arranged so that they provide a sorbent flow path that recirculates the sorbent between the first reactor system and the second reactor system.
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公开(公告)号:US20190151792A1
公开(公告)日:2019-05-23
申请号:US16258026
申请日:2019-01-25
IPC分类号: B01D53/04 , C10G25/00 , B01D53/12 , B01D53/08 , B01J20/20 , B01J20/02 , C10G25/09 , B01D53/02
CPC分类号: B01D53/0423 , B01D53/02 , B01D53/08 , B01D53/12 , B01D2253/102 , B01D2253/112 , B01D2253/25 , B01D2256/24 , B01D2257/306 , B01D2259/40083 , B01D2259/402 , B01J20/0225 , B01J20/0237 , B01J20/20 , C10G25/003 , C10G25/09 , C10G2300/202
摘要: A sulfur removal system including a first reactor and a second reactor that are located in series to one another each having an adsorbent that includes cobalt and copper on an activated carbon support, a method of desulfurizing a sulfur-containing hydrocarbon stream via the sulfur removal system, and a method of making the adsorbent. Various embodiments of the sulfur removal system, the desulfurizing method, and the method of making the adsorbent is also provided.
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4.
公开(公告)号:US20180326346A1
公开(公告)日:2018-11-15
申请号:US16042494
申请日:2018-07-23
发明人: Hal Stuhler , Lori Stuhler , Van T. Walworth , Scott Drummond
CPC分类号: B01D53/12 , B01D47/10 , B01D53/83 , B01D2253/102 , B01D2253/1128 , B01D2258/0283 , B01D2259/40084 , B01J8/26 , B01J8/36 , B01J20/0237 , B01J20/0244 , B01J20/0251 , B01J20/0285 , B01J20/3416 , B01J20/3433 , B01J2220/42 , B01J2220/56
摘要: An emissions control system including a fluidized bed apparatus containing a reactive sorbent material is disclosed for gaseous and non-gaseous contaminated emissions. The reactive sorbent material may be CZTS, CZTS-Alloy, or a carbon-based sorbent material. The fluidized bed apparatus is configured with one or more closed loop sorbent recycling subsystems. The sorbent recycling subsystems include the capability to separate sorbents from each other, separate contaminates from sorbents for disposal and/or recycling, clean and/or rejuvenate sorbents for return to the fluidized bed apparatus, dispose of spent and exhausted sorbents, and replace the spent and exhausted sorbents with new sorbent to maintain consistent sorbent function in the fluidized bed apparatus. Monitoring sensors provide information useful in a method for establishing and maintaining consistent process parameter controls.
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公开(公告)号:US20180311613A1
公开(公告)日:2018-11-01
申请号:US15772739
申请日:2016-11-02
申请人: DANIELI CORUS B.V.
CPC分类号: B01D53/83 , B01D53/10 , B01D53/12 , B01D53/40 , B01D53/44 , B01D2251/404 , B01D2253/102 , B01D2257/2045 , B01D2257/2047 , B01D2257/304 , B01D2257/60 , B01D2257/7027 , B01D2258/025 , B01D2259/128 , C10J3/00 , C10K1/024 , C10K1/20 , C10K1/32 , C21B7/002 , C21B2100/44 , C21C5/40 , C21C2100/02 , F27B1/10 , F27B3/10 , F27D17/008 , Y02P10/283
摘要: A process and a device for treating a flow of furnace gas with a pressure of more than 1 bar flowing through a channel. A powder agent, such as a powder comprising alkali reagents, such as lime, and/or absorbents, such as activated coal, is injected under an overpressure into the furnace gas flow via an injector which is positioned centrally within the channel The powder agent may be fluidized. The pressure for injecting the powder may be adjusted by controlling the volume of fluidization gas vented via a venting outlet.
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公开(公告)号:US20180272266A1
公开(公告)日:2018-09-27
申请号:US15525136
申请日:2015-11-03
申请人: SHELL OIL COMPANY
发明人: Gerald SPRACHMANN , Gerardus Antonius Franciscus VAN MOSSEL , Hendrik DATHE , Tobias PROELL , Gerhard SCHOENY
CPC分类号: B01D53/12 , B01D53/08 , B01D53/62 , B01D53/83 , B01D2252/204 , B01D2253/202 , B01D2257/504 , B01D2258/0283 , B01D2259/40086 , B01D2259/40096 , B01D2259/402 , B01D2259/65 , B01J8/189 , B01J8/26 , B01J20/22 , B01J20/28004 , B01J20/28011 , B01J20/28061 , B01J20/28064 , B01J20/28073 , B01J20/28076 , B01J20/3425 , B01J20/3466 , B01J20/3483 , Y02A50/2342 , Y02C10/04 , Y02C10/08
摘要: The present invention relates to a process for capturing carbon dioxide from a gas stream. The gas stream is contacted with solid adsorbent particles in an adsorption zone. The adsorption zone has at least two beds of fluidized solid adsorbent particles, and the solid adsorbent particles are flowing downwards from bed to bed. The solid adsorbent particles comprise 15 to 75 weight % of organic amine compounds. The gas stream entering the adsorption zone has a dew point which is at least 5° C. below the forward flow temperature of the coolest cooling medium in the adsorption zone. Carbon dioxide enriched solid adsorbent particles are heated, and then regenerated. The desorption zone has at least two beds of fluidized solid adsorbent particles, and the stripping gas is steam. The regenerated particles are cooled and recycled to the adsorption zone.
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公开(公告)号:US10011482B2
公开(公告)日:2018-07-03
申请号:US15430592
申请日:2017-02-13
发明人: Ravi Chandran , Daniel Michael Leo , Shawn Robert Freitas , Dave G. Newport , Hamilton Sean Michael Whitney , Daniel A. Burciaga
IPC分类号: C01B3/38 , C01B3/58 , C01B3/52 , C01B3/56 , B01D5/00 , B01D17/02 , B01D29/27 , B01D29/66 , B01D46/00 , B01D47/10 , B01D50/00 , B01D53/14 , B01D53/18 , B01D53/04 , B01D53/047 , B01D53/48 , B01D53/76 , B01D61/36
CPC分类号: C01B3/52 , B01D5/0027 , B01D5/006 , B01D5/0072 , B01D5/0075 , B01D5/009 , B01D17/0208 , B01D29/27 , B01D29/66 , B01D46/0036 , B01D47/10 , B01D50/006 , B01D53/0423 , B01D53/0462 , B01D53/047 , B01D53/0476 , B01D53/12 , B01D53/1406 , B01D53/1412 , B01D53/1431 , B01D53/1462 , B01D53/1468 , B01D53/1487 , B01D53/18 , B01D53/265 , B01D53/326 , B01D53/48 , B01D53/76 , B01D61/362 , B01D2252/102 , B01D2252/103 , B01D2252/20436 , B01D2252/504 , B01D2252/602 , B01D2256/16 , B01D2256/20 , B01D2257/304 , B01D2257/306 , B01D2257/406 , B01D2257/504 , B01D2257/60 , B01D2257/708 , B01D2259/402 , C01B3/24 , C01B3/38 , C01B3/382 , C01B3/386 , C01B3/56 , C01B3/58 , C01B2203/0227 , C01B2203/0233 , C01B2203/025 , C01B2203/0261 , C01B2203/04 , C01B2203/0415 , C01B2203/042 , C01B2203/043 , C01B2203/0435 , C01B2203/045 , C01B2203/0465 , C01B2203/0475 , C01B2203/048 , C01B2203/0485 , C01B2203/061 , C01B2203/062 , C01B2203/068 , C01B2203/0877 , C01B2203/1235 , C01B2203/1241 , C01B2203/142 , C01B2203/147 , C01B2203/84 , H05K999/99 , Y02P20/13 , Y02P30/30
摘要: A system and method for processing unconditioned syngas first removes solids and semi-volatile organic compounds (SVOC), then removes volatile organic compounds (VOC), and then removes at least one sulfur containing compound from the syngas. Additional processing may be performed depending on such factors as the source of syngas being processed, the products, byproducts and intermediate products desired to be formed, captured or recycled and environmental considerations.
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公开(公告)号:US20180169579A1
公开(公告)日:2018-06-21
申请号:US15557239
申请日:2015-03-11
发明人: Markus FELDKAMP , Markus DICKAMP , Tianjing LI , Lars PRIEBE , Christian MOSER
CPC分类号: B01D53/83 , B01D53/12 , B01D53/50 , B01D53/508 , B01D53/685 , B01D53/70 , B01D2251/404 , B01D2251/602 , B01D2251/604 , B01D2257/2045 , B01D2257/2047 , B01D2257/2064 , B01D2257/2066 , B01D2257/602
摘要: The invention relates to a method for cleaning flue gas, the flue gas to be cleaned and a sorption agent starting material in the form of a solid being injected into a reactor chamber of a fluidized-bed reactor, and a liquid being injected into the reactor chamber separately from the flue gas and the sorption agent starting material, the sorption agent starting material being contacted with the liquid in the fluidized-bed reactor and being converted to a sorption agent in the form of a solid.
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公开(公告)号:US20180169574A1
公开(公告)日:2018-06-21
申请号:US15574965
申请日:2016-05-18
发明人: Surajit SENGUPTA , Vinay AMTE , Asit Kumar DAS , Satyanarayana Reddy AKURI , Manoj YADAV , Sukumar MANDAL , Amit GOHEL , Sampath NERIVETLA , Kalyan Chandra NATH
CPC分类号: B01D53/62 , B01D53/12 , B01D53/96 , B01D2251/306 , B01D2251/606 , B01D2253/104 , B01D2253/106 , B01D2253/112 , B01D2253/304 , B01D2257/504 , B01D2258/06 , B01D2259/4009 , B01J20/043 , B01J20/08 , B01J20/16 , B01J20/28061 , B01J20/28064 , B01J20/28069 , B01J20/3204 , B01J20/3225 , B01J20/3236 , B01J20/3433 , B01J20/3458 , Y02A50/2342 , Y02C10/04 , Y02C10/08
摘要: The present disclosure relates to a process for capturing carbon-dioxide from a gas stream. In order to capture the carbon-dioxide, a support is provided and potassium carbonate (K2CO3) is impregnated thereon to form an adsorbent comprising potassium carbonate (K2CO3) impregnated support. The adsorbent is activated to form an activated adsorbent. The gas stream is passed through the adsorber to enable adsorption of the carbon-dioxide on the activated adsorbent to form a carbon-dioxide laden adsorbent. The carbon-dioxide laden adsorbent is transferred to a desorber for at least partially desorbing the carbon-dioxide from the carbon-dioxide laden adsorbent by passing a carbon-dioxide deficient stream through the desorber. The partially regenerated adsorbent is returned to the adsorber for adsorbing the carbon-dioxide from the carbon-dioxide. The process of the present disclosure reduces the overall energy demand by partially regenerating the adsorbent.
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公开(公告)号:US09895647B2
公开(公告)日:2018-02-20
申请号:US14731598
申请日:2015-06-05
发明人: Yau-Pin Chyou , Po-Chuang Chen , Hung-Te Hsu , Keng-Tung Wu
CPC分类号: B01D53/12 , B01D53/346 , B01D53/62 , B01D53/83 , B01D2257/504 , B01D2258/0283 , B01J8/34 , B01J8/36 , Y02C10/04
摘要: The present invention provides a method for dynamically controlling the circulation rate of solids in an interconnected fluidized bed. When an interconnected fluidized bed is operating, it is available to control the circulation rate of solids by adopting the steps of adjusting the height difference between the orifice on the weir and the bottom surface of the bed region, adjusting the cross-sectional area of the above orifice, or adjusting the height of the above weir. By using multiple ways, the circulation rate of solids can be improved substantially. In addition, the curve of circulation rate of solids can be converged to the maximum circulation rate of solids effectively.
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