-
1.发明公开公开(公告)号：US20240246052A1
公开(公告)日：2024-07-25
申请号：US18566128
申请日：2022-06-23
申请人： CHINA PETROLEUM & CHEMICAL CORPORATION , SHANGHAI RESEARCH INSTITUTE OF PETROCHEMICAL TECHNOLOGY, SINOPEC
发明人： Hongyuan ZONG , Guozhen QI , Pan GAO , Xiaohong LI , Jing CAO , Zhinan YU , Yanxue WANG , Fei PENG
CPC分类号： B01J8/1827 , B01J8/0055 , B01J8/1863 , B01J8/26 , C07C1/24 , B01J2208/00752 , B01J2208/00849 , B01J2208/00902 , B01J2208/00938 , C07C2529/40
摘要： A fluidized bed reactor, a device for preparing low-carbon olefin, and a method for preparing low-carbon olefin are provided. The reaction zone of the fluidized bed reactor is sequentially, from bottom to top, provided with a raw material first distributor, a raw material second distributor and a catalyst distributor; the catalyst distributor is connected with the catalyst second feeding inlet; a dense-phase zone is formed between the raw material first distributor and the raw material second distributor, and the area where the catalyst distributor is located is formed as a catalyst distribution zone connected with the dense-phase zone; and at least one catalyst first feeding inlet(s) is provided on the side wall of reactor of the dense-phase zone. The distribution of the catalyst and the full contact of the catalyst with the raw materials can be achieved using the fluidized bed reactor and the device.
-
公开(公告)号：US11993516B2
公开(公告)日：2024-05-28
申请号：US17626781
申请日：2020-11-30
申请人： LG CHEM, LTD.
发明人： Yon Jee Kim , Kwang Woo Yoon , Og Sin Kim , Se Hyun Kim , Seung Yong Lee
CPC分类号： C01B32/16 , B01J8/005 , B01J8/1809 , B01J8/1863 , B01J8/1872 , B82Y40/00 , B01J2219/0031 , C01B2202/26 , C01B2202/36
摘要： In the present invention, only low-growth carbon nanotubes are selectively separated among solid particles discharged during a reaction and then re-input to a reactor, so that it is possible to improve the quality of a carbon nanotube product to be produced and the productivity of a carbon nanotube production process.
-
公开(公告)号：US10011791B2
公开(公告)日：2018-07-03
申请号：US14525755
申请日：2014-10-28
申请人： UOP LLC
IPC分类号： B01J8/24 , C10G75/02 , B01J8/18 , B01J8/26 , B01J8/28 , B01J8/38 , B01J19/02 , B01J8/00 , C10G11/18 , B01J38/30 , B01J29/90
CPC分类号： C10G75/02 , B01J8/0015 , B01J8/002 , B01J8/003 , B01J8/0055 , B01J8/1863 , B01J8/26 , B01J8/28 , B01J8/388 , B01J19/02 , B01J29/90 , B01J38/30 , B01J2208/00849 , B01J2208/00902 , B01J2208/00911 , B01J2208/00991 , B01J2219/024 , B01J2219/0245 , C10G11/182
摘要： Methods and apparatuses for regenerating catalysts and methods of inhibiting corrosion in catalyst regenerating apparatuses are provided. An exemplary apparatus includes: a metal vessel configured to receive a spent catalyst stream and contact at least a portion of the spent catalyst stream with an oxygen containing environment at a sufficiently high temperature to burn coke present in the spent catalyst stream; a refractory material overlying at least a portion of an inner surface of the metal vessel; and a corrosion inhibiting material in contact with at least a portion of the inner surface of the metal vessel and disposed between the inner surface and at least a portion of the refractory material, wherein the corrosion inhibiting material is heat stable at a temperature of at least up to about 400° F. (about 204° C.) and inhibits contact of an acid environment with the inner surface of the metal vessel.
-
4.发明申请公开(公告)号：US20180169602A1
公开(公告)日：2018-06-21
申请号：US15825174
申请日：2017-11-29
发明人： Mohsen N. Harandi , Alvin U. Chen , Charles R. Bolz , Christopher G. Smalley , Masaaki Sugita , Suriyanarayanan Rajagopalan , Bing Du
CPC分类号： B01J8/26 , B01J8/1863 , B01J8/1872 , B01J8/30 , B01J8/388 , B01J29/40 , B01J29/90 , B01J38/14 , C07C2/12 , C10G11/182 , C10G2300/1092 , C10G2300/708 , C10G2400/02
摘要： A method is provided for upgrading a hydrocarbon feed. The method may include contacting a hydrocarbon feed with a catalyst in a fluidized bed reactor; directing a portion of the catalyst from the fluidized bed reactor to a regeneration zone, such that the portion of the catalyst flows in a first direction through the regeneration zone; directing combustion air into the regeneration zone in a counter-flow direction to the first direction, wherein the combustion air is provided at a rate of about 100.05% or less of the stoichiometric air requirement for combusting coke present on the portion of catalyst; regenerating the portion of the catalyst in the regeneration zone to produce regenerated catalyst; and directing a portion of the hydrocarbon feed to combine with the regenerated catalyst downstream of the regeneration zone and lift the regenerated catalyst back to the fluidized bed reactor.
-
5.发明申请公开(公告)号：US20180079973A1
公开(公告)日：2018-03-22
申请号：US15706348
申请日：2017-09-15
发明人： Liang Chen , Peter Loezos , Rama Rao Marri , Bryan Tomsula , Jon A. Hood , Hardik Singh , Michael Dorsey , Justin Breckenridge
CPC分类号： C10G51/026 , B01D45/06 , B01D45/08 , B01J8/0055 , B01J8/0065 , B01J8/1845 , B01J8/1863 , B01J8/24 , B01J8/26 , B01J2208/00362 , B01J2208/0038 , B01J2208/00752 , B01J2208/00761 , B01J2208/00991 , C10G11/18 , C10G2400/20 , C10G2400/30
摘要： Apparatus and processes herein provide for converting hydrocarbon feeds to light olefins and other hydrocarbons. The processes and apparatus include, in some embodiments, feeding a hydrocarbon, a first catalyst and a second catalyst to a reactor, wherein the first catalyst has a smaller average particle size and is less dense than the second catalyst. A first portion of the second catalyst may be recovered as a bottoms product from the reactor, and a cracked hydrocarbon effluent, a second portion of the second catalyst, and the first catalyst may be recovered as an overhead product from the reactor. The second portion of the second catalyst may be separated from the overhead product, providing a first stream comprising the first catalyst and the hydrocarbon effluent and a second stream comprising the separated second catalyst, allowing return of the separated second catalyst in the second stream to the reactor.
-
公开(公告)号：US20180066195A1
公开(公告)日：2018-03-08
申请号：US15553797
申请日：2016-02-23
发明人： Mustapha N. Karime
CPC分类号： C10G11/182 , B01J8/0025 , B01J8/003 , B01J8/0055 , B01J8/1863 , B01J8/1872 , B01J8/26 , B01J8/388 , B01J2208/00061 , B01J2208/0007 , B01J2208/00539 , B01J2208/00575 , B01J2208/00592 , B01J2208/00628 , B01J2208/00707 , C07C5/333 , C10G11/18 , Y02P20/584 , C07C11/09
摘要： The presently disclosed subject matter relates to systems and methods for catalyst regeneration. In particular, the presently disclosed subject matter provides for an integrated fluidized bed reactor and catalyst regeneration system to minimize hydrocarbon accumulation. In one embodiment, the presently disclosed subject matter provides for a fluidized bed reactor unit including a catalyst riser having a partially perforated surface in close proximity to a reactor stripper.
-
公开(公告)号：US20170369311A1
公开(公告)日：2017-12-28
申请号：US15542704
申请日：2016-02-04
发明人： Aghaddin MAMEDOV
CPC分类号： C01B3/40 , B01J8/003 , B01J8/02 , B01J8/1863 , B01J8/26 , B01J23/002 , B01J23/34 , B01J23/755 , B01J23/78 , B01J23/83 , B01J23/8892 , B01J23/892 , B01J23/94 , B01J35/023 , B01J38/12 , B01J2208/02 , B01J2523/00 , C01B2203/0238 , C01B2203/1041 , C01B2203/1058 , C01B2203/1082 , C01B2203/1241 , Y02P20/52 , Y02P20/584
摘要： Methods and systems for converting methane to syngas are provided. Certain exemplary methods and systems involve reacting methane and carbon dioxide with a nickel oxide catalyst in a reaction chamber, thereby providing syngas and a reduced nickel species. The reduced nickel species can be regenerated by oxidation with air in a regeneration chamber, thereby generating a regenerated nickel oxide and heat. The regenerated nickel oxide and heat can be returned to the reaction chamber to drive the syngas reaction.
-
公开(公告)号：US20170267933A1
公开(公告)日：2017-09-21
申请号：US15507899
申请日：2015-01-21
申请人： Baozhen SHI
发明人： Baozhen SHI
CPC分类号： C10G11/00 , B01J8/001 , B01J8/003 , B01J8/0035 , B01J8/0055 , B01J8/1809 , B01J8/1836 , B01J8/1863 , B01J8/24 , B01J8/26 , B01J38/12 , B01J38/34 , B01J2208/0038 , C10G2300/70 , C10G2300/708
摘要： A regeneration method for catalytic cracking reaction, the method is applied in a catalytic reaction process of petroleum hydrocarbon materials, and the method comprises: feeding the regenerated and semi-regenerated catalyst from a regenerator separately into different positions of a reactor for reaction. A part of the semi-regenerated catalyst is firstly processed in a purification cooler for removing carried nitrogen, oxygen, carbon dioxide and impurity gases before being fed into the reactor. Spent catalyst or the purified and cooled semi-regenerated catalyst is fed into a catalyst mixing section of the reactor for controlling the temperature of the catalyst being contact with the oil material to be gasified, thereby achieving a three stage cycle of the catalyst in the reactor and a three stage control for the reaction outlets of the oil material gasification zone and the cracking reaction zone and the catalyst taking part in the reaction.
-
公开(公告)号：US09725374B2
公开(公告)日：2017-08-08
申请号：US14540856
申请日：2014-11-13
发明人： Ho-jung Ryu , Dong-ho Lee , Gyoung-tae Jin , Do-won Shun , Chang-keun Yi , Jae-hyeon Park , Dal-hee Bae , Sung-ho Jo , Seung-yong Lee , YoungCheol Park , Jong-ho Moon , Ji-bong Joo
CPC分类号： C07C1/042 , B01J8/0015 , B01J8/005 , B01J8/0055 , B01J8/12 , B01J8/1809 , B01J8/1818 , B01J8/1827 , B01J8/1836 , B01J8/1863 , B01J8/1872 , B01J8/26 , B01J8/28 , B01J8/388 , B01J2208/00132 , B01J2208/0053 , B01J2208/00752 , B01J2208/00761 , C07C1/0415 , C07C1/045 , C07C1/049 , C10L3/08 , C10L2290/06 , C10L2290/10 , C10L2290/12 , C10L2290/42
摘要： A system for preventing a catalyst from overheating is provided. The system includes: a first reactor filled with a catalyst at least in part and configured to receive reaction gas and produce product gas; and a second reactor configured to cool a catalyst discharged from the first reactor. The catalyst is circulated between the first reactor and the second reactor by injecting the catalyst cooled in the second reactor into the first rector.
-
公开(公告)号：US20160264890A1
公开(公告)日：2016-09-15
申请号：US14642990
申请日：2015-03-10
申请人： UOP LLC
发明人： Jibreel A. Qafisheh
CPC分类号： C10G69/04 , B01J8/003 , B01J8/0055 , B01J8/18 , B01J8/1827 , B01J8/1845 , B01J8/1863 , B01J8/26 , B01J2208/00176 , B01J2208/00796 , B01J2208/00902 , B01J2208/00911 , C10G11/18 , C10G55/06 , C10G2300/4081
摘要： A process and apparatus is for recycling LCO and/or HCO to an FCC unit to recover additional distillate. Spent catalyst recycle in the FCC unit may be used to improve distillate yield. A hydroprocessing zone may saturate cycle oil aromatics for cracking in an FCC unit. The recycle cracked stream may be recycled to a downstream hydroprocessing zone to avoid a first hydroprocessing zone for hydrotreating feed to the FCC unit. Additional recovery of cycle oil for recycle is obtained by heating slurry oil prior to vacuum separation.
摘要翻译： 一种方法和设备是将LCO和/或HCO再循环到FCC单元以回收另外的馏出物。 可以使用FCC装置中的废催化剂再循环来提高馏出物的产率。 加氢处理区可能会使FCC油循环油芳族化合物在FCC装置中饱和。 再循环裂化的物流可以循环到下游加氢处理区，以避免用于将进料加氢至FCC单元的第一加氢处理区。 通过在真空分离之前加热浆料油来获得用于再循环的循环油的额外回收。
-
-
-
-
-
-
-
-
-
搜索结果
380 条记录 (耗时 0.024 秒)
