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131.
公开(公告)号:US20220203340A1
公开(公告)日:2022-06-30
申请号:US17137576
申请日:2020-12-30
申请人: UOP LLC
发明人: Avram M. Buchbinder , Wei Pan , J. W. Adriaan Sachtler , Jeffrey M. Noga , Xi Zhao , Ling Zhou , John A. Karch
IPC分类号: B01J23/62 , B01J23/58 , B01J21/04 , B01J21/12 , B01J21/06 , B01J35/02 , B01J35/10 , B01J35/00 , B01J23/96 , B01J38/30 , B01J8/18 , B01J8/26 , C07C5/48
摘要: A process is provided for dehydrogenating a paraffinic hydrocarbon comprising sending the paraffinic hydrocarbon to a fluidized bed reactor to be contacted at dehydrogenation reaction conditions with a catalyst composition comprising less than about 0.0999 wt % platinum and about 0.05-2.5 wt % Group I or Group II elements or a mixture thereof. The catalytic composition is prepared without addition of tin, gallium, indium, germanium or lead.
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132.
公开(公告)号:US11060038B2
公开(公告)日:2021-07-13
申请号:US16751030
申请日:2020-01-23
发明人: Marc Bories , Patrick Leroy , Eusebius Gbordzoe
IPC分类号: B01J8/26 , B01J8/32 , B01J8/34 , C10G11/18 , B01J38/30 , B01J38/02 , B01J8/00 , B01J8/24 , C07C4/06
摘要: The present invention discloses a process for the catalytic cracking of a weakly coking feedstock having a Conradson carbon residue of 0.1% by weight and a hydrogen content of greater than 12.7% by weight, comprising at least a feedstock cracking zone, a zone for separating/stripping the effluents from the coked catalyst particles and a zone for regenerating said particles, characterized in that at least a solid carbon material in the fluidized state, having a carbon content equal to or greater than 80% by weight, is injected upstream of and/or during the catalyst regeneration step into a dense bed of coked catalyst.
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公开(公告)号:US20210189258A1
公开(公告)日:2021-06-24
申请号:US17054345
申请日:2019-05-10
申请人: KOREA INSTITUTE OF MACHINERY & MATERIALS , CENTER KOREA RESEARCH INSTITUTE OF CHEMICAL TECHNOLOGY
发明人: Sungkwon JO , Seongil CHOI , Donghyun CHO , Dae-hoon LEE , Kwan-Tae KIM , Younghoon SONG , Yong-Ki PARK , Na Young KANG
摘要: A catalyst regenerator according to an embodiment of the present invention, as a catalyst regenerator that regenerates a coked catalyst separated from a product produced in an endothermic catalytic reaction of a fluidized bed reactor, includes: a reaction chamber that includes a regeneration space, receives the coked catalyst from a standpipe connected to the regeneration space, and discharges a regenerated catalyst to an outlet; a fuel supplier that is connected to the reaction chamber to inject a fuel for combustion into the regeneration space; and a fuel supplier that is connected to the reaction chamber to inject an air for combustion into the regeneration space, wherein the fuel injected from the fuel supplier is a reformed fuel containing hydrogen and carbon monoxide.
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公开(公告)号:US10646863B2
公开(公告)日:2020-05-12
申请号:US15918678
申请日:2018-03-12
发明人: Shoeb Hussain Khan , Vikas Badhan , Venkata Hari Prasad Gupta Bandaru , Gautam Thapa , Satheesh Vetterkunnel Kumaran , Debasis Bhattacharyya , Sankara Sri Venkata Ramakumar
摘要: A spent catalyst distributor for distributing spent catalyst in a catalyst regenerator vessel housing a dense phase catalyst bed and a dilute phase catalyst bed. The spent catalyst distributor comprises a conduit comprising a proximal end and a distal end. The conduit projects horizontally or horizontally and downwardly into the regenerator vessel and includes an opening located at the distal end for introducing the spent catalyst at a first location inside the regenerator vessel. The conduit further includes a plurality of orifices located along a length of the conduit between the distal end and an inner wall of the regenerator vessel for introducing the spent catalyst at a plurality of locations inside the regenerator vessel.
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公开(公告)号:US20200055015A1
公开(公告)日:2020-02-20
申请号:US16609905
申请日:2018-05-03
发明人: Matthew T. Pretz
摘要: A method for processing a chemical stream includes contacting a feed stream with a catalyst in a reactor portion of a reactor system causing a reaction which forms a product stream. The method includes separating the product stream from the catalyst, passing the catalyst to a catalyst processing portion of the reactor system, processing the catalyst in the catalyst processing portion, and passing a portion of the catalyst from the catalyst processing portion of the reactor system into a catalyst withdrawal system that includes a catalyst withdrawal vessel and a transfer line coupling the catalyst withdrawal vessel to the catalyst processing portion. Each of the catalyst withdrawal vessel and the transfer line include an outer metallic shell and an inner refractory lining. The method further includes cooling the catalyst in the catalyst withdrawal vessel from greater than or equal to 680° C. to less than or equal to 350° C.
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公开(公告)号:US10464036B2
公开(公告)日:2019-11-05
申请号:US15761557
申请日:2016-09-28
摘要: A catalyst regenerator for combusting carbonaceous deposits from a catalyst comprising a first chamber which comprises a catalyst inlet for feeding spent catalyst with carbonaceous deposits to said first chamber, a supplemental fuel gas distributor, and a distributor for an oxygen containing gas for distributing oxygen containing gas into said first chamber to contact said spent catalyst and combust carbonaceous deposits and supplemental fuel which further deactivates the spent catalyst and generates flue gas; a riser section extending from said first chamber for transporting the spent catalyst and the flue gas, the riser section comprising an outer wall, at least one slot in the outer wall, and a riser termination device which comprises a substantially internally flat cover plate, at least one arm extending from the cover plate, wherein the arm extends about the slot from the outer wall, the arm comprising an outer shell that encloses the arm and wherein no internal portion of the cover plate extends above an upper surface of the outer shell of the at least one arm is provided. Further provided is a riser termination device.
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公开(公告)号:US20180185807A1
公开(公告)日:2018-07-05
申请号:US15740035
申请日:2016-06-28
申请人: SHELL OIL COMPANY
发明人: Cian Seamus CARROLL
CPC分类号: B01J8/1872 , B01J8/0025 , B01J8/008 , B01J8/1818 , B01J8/1827 , B01J8/1863 , B01J38/30 , B01J2208/00752 , B01J2208/00769 , B01J2208/00831 , B01J2208/0084 , C10G11/182
摘要: A catalyst standpipe comprising a horizontal section, a sloped section, and vertical section, wherein the vertical section comprises one or more ring portions and associated methods and systems.
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公开(公告)号:US09895676B2
公开(公告)日:2018-02-20
申请号:US14398891
申请日:2013-05-06
IPC分类号: B01J21/16 , B01J8/08 , B01J8/12 , B01J8/18 , C07C1/26 , B01J37/04 , B01J23/02 , B01J29/08 , B01J35/00 , B01J35/02 , B01J35/10 , B01J37/00 , B01J37/14 , C07C1/30 , B01J37/06 , B01J37/08 , B01J38/30 , B01J23/06 , B01J23/92 , B01J29/90 , B01J35/08
CPC分类号: B01J21/16 , B01J8/085 , B01J8/125 , B01J8/1809 , B01J23/02 , B01J23/06 , B01J23/92 , B01J29/082 , B01J29/90 , B01J35/0006 , B01J35/002 , B01J35/0093 , B01J35/023 , B01J35/026 , B01J35/08 , B01J35/1061 , B01J35/1066 , B01J37/0009 , B01J37/0018 , B01J37/0063 , B01J37/0072 , B01J37/04 , B01J37/06 , B01J37/086 , B01J37/088 , B01J37/14 , B01J38/30 , B01J2208/00274 , C07C1/26 , C07C1/30 , C07C2521/10 , C07C2521/16 , C07C2527/232 , Y02P20/584 , C07C11/02 , C07C11/08
摘要: Generally, regenerable, encapsulated metal oxide catalysts comprising a ceramic matrix and metal catalysts may be used to convert alkanes to alkenes. The encapsulated metal oxide catalyst may be tailored to produce a variety of alkenes including ethylene, butylene, and propylene. Further, the encapsulated metal oxide catalysts advantageously allow for regeneration and reactant recovery for cost effective and environmentally friendly processes.
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139.
公开(公告)号:US09718743B2
公开(公告)日:2017-08-01
申请号:US15100834
申请日:2013-12-03
发明人: Zhongmin Liu , Mao Ye , Tao Zhang , Changqing He , Xiangao Wang , Yinfeng Zhao
IPC分类号: C07C1/20 , C07C1/207 , C07C1/213 , C07C1/24 , C07C1/247 , B01J38/30 , B01J38/34 , B01J8/26 , B01J8/18 , B01J29/85 , B01J29/90 , B01J38/06 , B01J38/12
CPC分类号: C07C1/20 , B01J8/1827 , B01J8/1836 , B01J8/1872 , B01J8/26 , B01J8/34 , B01J8/36 , B01J29/85 , B01J29/90 , B01J38/06 , B01J38/12 , B01J2208/00141 , B01J2208/00902 , C07C2529/85 , Y02P20/584 , Y02P30/42 , C07C11/02
摘要: A method for preparing a light olefin using an oxygen-containing compound, and a device for use thereof, more specifically, taking methanol and/or dimethyl ether as main starting materials, using a multi-stage (n≧2) dense phase fluidized bed reactor and a multi-stage (m≧2) catalyst regenerator, which solves the problem in the prior art of the uniformity of catalyst carbon deposition and the carbon content being difficult to control and the light olefin selectivity being low.
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公开(公告)号:US20160362614A1
公开(公告)日:2016-12-15
申请号:US15156637
申请日:2016-05-17
CPC分类号: C10G11/18 , B01J8/24 , B01J38/14 , B01J38/36 , B01J2208/00752 , C10G11/182 , C10G2300/4093 , C10G2300/70
摘要: An FCC unit enables the normal regenerator to be eliminated by carrying out catalyst regeneration in the reactor section of the unit using air, oxygen-enriched air or even relatively pure oxygen as the stripping medium in the stripping section of the reactor while maintaining overall reducing conditions so that sulfur and nitrogen are produced in the form of hydrogen sulfide, ammonia and other reduced species. The combustion gases from the stripper are sent from the reactor with the cracking vapors to the FCC main fractionator, wet gas compressor and gas plant to process the by-products of the coke combustion along with the FCC reactor effluent. The principle is applicable to grass-roots FCC units with its potential for elimination of a major unit component but it also has potential for application to existing units to reduce the load on the regenerator or eliminate the need for the existing regenerator so that an existing regenerator may be converted to a parallel or auxiliary reactor system.
摘要翻译: FCC装置使得能够通过在反应器部分中进行催化剂再生来消除正常的再生器,所述反应器部分使用空气,富氧空气或甚至相对纯的氧作为反应器的汽提部分中的汽提介质,同时保持总体还原条件 使得硫和氮以硫化氢,氨等还原物质的形式产生。 来自汽提器的燃烧气体从具有裂解蒸汽的反应器送入FCC主分馏器,湿气压缩机和气体设备,以与FCC反应器流出物一起处理焦炭燃烧的副产物。 该原则适用于具有消除主要单元组件的潜力的基层FCC单元,但它也具有应用于现有单元以减少再生器负载的潜力,或者消除对现有再生器的需要,使得现有的再生器 可以转换为并联或辅助反应器系统。
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