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公开(公告)号：US4325916A
公开(公告)日：1982-04-20
申请号：US108409
申请日：1979-12-31
Applicant: Arthur C. Worley
Inventor： Arthur C. Worley
CPC classification number: C01B3/384 , B01J8/08 , C01B2203/0233 , C01B2203/0238 , C01B2203/0816 , C01B2203/1011 , C01B2203/1052 , C01B2203/1082 , C01B2203/1235 , Y02P20/142
Abstract: A hydrocarbon reformer furnace is provided having a plurality of vertical tubes running through a furnace firebox wherein the upper and lower ends of said tubes are connected to inlet and outlet headers respectively. The apertures through which the lower ends of the vertical tubes exit the firebox are sealed with cast-in-place refractory seals to provide an air seal and mechanical dampening of said tubes.
Abstract translation: 提供一种烃重整炉，其具有穿过炉火炉的多个垂直管，其中所述管的上端和下端分别连接到入口和出口集管。 垂直管的下端离开火炉的孔通过现浇耐火密封件密封，以提供所述管的空气密封和机械阻尼。
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公开(公告)号：US4243794A
公开(公告)日：1981-01-06
申请号：US949956
申请日：1978-10-10
Applicant: James L. White , James G. Berg
Inventor： James L. White , James G. Berg
CPC classification number: B01J8/08 , C08J3/12 , C09D5/031 , Y10S525/934
Abstract: Free flowing resin powder which upon striking a heated article fuses, flows and hardens to provide a protective coating, which powder consists of a mixture of rough and rounded particles, the rough particles having a granular appearance as a result of being pulverized and the rounded particles having smooth, glossy, spheroidized surfaces as a result of being briefly heated to a temperature above the softening point. Preferably each particle of the powder is a blend of thermosetting resin and curing agent.
Abstract translation: 自由流动的树脂粉末在被加热的物体上熔化，流动并硬化以提供保护涂层，该粉末由粗糙和圆形颗粒的混合物组成，粗糙颗粒具有被粉碎的颗粒状外观和圆形颗粒 由于短暂加热到高于软化点的温度，具有光滑，有光泽，球化的表面。 优选地，粉末的每个颗粒是热固性树脂和固化剂的共混物。
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公开(公告)号：US3348941A
公开(公告)日：1967-10-24
申请号：US39660364
申请日：1964-09-15
Applicant: NORTHERN NATURAL GAS CO , W S MOORE COMPANY
Inventor： KING RICHARD E
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公开(公告)号：US2461172A
公开(公告)日：1949-02-08
申请号：US75401847
申请日：1947-06-11
Applicant: SINCLAIR REFINING CO
Inventor： LOUIS PELZER HARRY
IPC: B01J8/08
CPC classification number: B01J8/08
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Patent Agency Ranking
66.发明授权公开(公告)号：US12018102B2
公开(公告)日：2024-06-25
申请号：US17051204
申请日：2019-05-29
Applicant: BOREALIS AG
Inventor： Apostolos Krallis , Vasileios Kanellopoulos , Erno Elovainio , Klaus Nyfors
CPC classification number: C08F2/34 , B01J8/0055 , B01J8/08 , B01J8/1827 , B01J8/1872 , B01J8/24 , C08F10/02 , C08F210/16 , C08F210/16 , C08F210/08 , C08F2500/24 , C08F110/02 , C08F2/001 , C08F110/02 , C08F4/6492
Abstract: The present invention relates to a process for polymerizing at least one olefin in gas phase in a fluidized bed in a polymerization reactor having a top zone of a generally conical shape as such that the equivalent cross-sectional diameter is monotonically decreasing with respect to the flow direction of the fluidization gas, a middle zone in direct contact with and below said top zone of a generally cylindrical shape and a bottom zone in direct contact and below said middle zone and of a generally conical shape as such that the equivalent cross-sectional diameter is monotonically increasing with respect to the flow direction of the fluidization gas, comprising the steps of: a) introducing a first stream of fluidization gas into the bottom zone; b) polymerizing at least one olefin in the presence of a polymerization catalyst in the fluidized bed formed by particles of a polymer of the at least one olefin suspended in an upwards flowing stream of the fluidization gas in the middle zone; c) withdrawing a second stream comprising the fluidization gas and optionally particles of a polymer of the at least one olefin from the top zone; characterized in that the temperature of the particles of the polymer of the at least one olefin in the fluidized bed (TPP) does not exceed 120% of the operating temperature set point (TS) of the polymerization reactor, wherein TPP and TS are both given in ° C., and the use of said process for polymerizing an olefin homo- or copolymer having a narrow particle size distribution.
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67.发明公开公开(公告)号：US20230241679A1
公开(公告)日：2023-08-03
申请号：US18003457
申请日：2021-06-29
Applicant: OHIO STATE INNOVATION FOUNDATION
Inventor： Liang-Shih Fan , Andrew Tong , Liang Zeng , Yitao Zhang , Frank Kong , Yu-Yen Chen
CPC classification number: B22F9/22 , B01J8/08 , B22F1/145 , B01J6/008 , B01J8/003 , B22F2302/25 , B22F2201/04 , B22F2201/013 , B01J2208/00628 , B01J2208/00761
Abstract: Reactor configurations may include one or more staged inlets and/or one or more staged outlets for gaseous and solid feedstocks. In one embodiment of the present disclosure, a reactor design for gas-solid reaction with one or more additional outlet for gas and/or solid phase is provided. In yet another embodiment, the design for a gas-solid reactor with one side inlet and two outlets for gas phase is described. In one embodiment, a reactor design with pairs of inlet and outlet for both gas and solid phase is provided. In another embodiment, a reactor design with one or more side inlets but only one outlet for gas phase is provided. In yet another embodiment, a reactor design with two inlets at the top/bottom of reactor and two side outlets for gaseous phase is described. In yet another embodiment, a reactor design with one or more side inlets and outlets for both gas and solid phases is provided.
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68.发明授权公开(公告)号：US10071939B2
公开(公告)日：2018-09-11
申请号：US14636297
申请日：2015-03-03
Applicant: Saudi Arabian Oil Company
Inventor： Raed Abudawoud
IPC: B01J8/00 , B01J8/08 , B01J8/18 , B01J8/24 , B01J19/00 , B01J19/24 , C07C4/18 , C07C6/06 , C07C6/12 , C07C4/12 , C10G65/04
CPC classification number: C07C4/18 , B01J8/08 , B01J8/24 , B01J2219/24 , C07C4/12 , C07C6/06 , C07C6/123 , C07C6/126 , C07C2529/40 , C07C2529/70 , C10G65/043 , C10G2400/30 , C07C15/06 , C07C15/02 , C07C15/08
Abstract: The present invention relates to a method of forming mixed xylenes from a heavy reformate using a dealkylation-transalkylation system that includes the step of introducing a heavy reformate containing methyl ethyl benzenes and tri-methyl benzenes and sufficiently free of toluene into the dealkylation stage with a hydrogen-containing material such that the heavy reformate and the hydrogen-containing material intermingle and contact a hydrodealkylation catalyst. The dealkylation-transalkylation system includes dealkylation stages, non-aromatic product gas separations and transalkylation stages. The BTEX component toluene forms from the reaction of methyl ethyl benzenes and hydrogen in the presence of the hydrodealkylation catalyst. The method also includes the step of introducing a dealkylated heavy reformate into the transalkylation stage such that the dealkylated heavy reformate contacts a transalkylation catalyst, forming a transalkylation stage product mixture that includes mixed xylenes.
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69.发明授权公开(公告)号：US10010845B2
公开(公告)日：2018-07-03
申请号：US15335592
申请日：2016-10-27
Inventor： Yau-Pin Chyou , Po-Chuang Chen , Hsiu-Yun Chien , Keng-Tung Wu , Ching-Ying Huang
CPC classification number: B01J8/08 , B01J8/087 , B01J8/26 , B01J2208/00256 , C01B32/50 , F23C10/10 , F23C2900/99008 , Y02E20/346
Abstract: An apparatus of hydrocarbon fuel reactors separates and purifies carbon dioxide (CO2). Interconnected fluidized beds are applied in chemical-looping combustion. A multi-stage reduction reaction is processed with iron-based oxygen carriers. Three reduction stages using the iron-based oxygen carriers are accurately and completely controlled. Each of the three stages is separately processed in an individual space. Oxygen in the iron-based oxygen carriers can be fully released. High-purity CO2 is obtained. Hydrogen can be produced as an option. Horizontal connection of three reduction reactors is changed into vertical one. An oxidation reactor is further connected. Thus, the whole structure occupies less area and effectively uses vertical space. Not only small space is effectively used; but also high-volume capacity is obtained. Each of the reactors has better geometry flexibility. The tandem reactor in each layer has less geometric influence and limitation. Therefore, each of the reactors can be resized on its own.
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公开(公告)号：US09920261B2
公开(公告)日：2018-03-20
申请号：US13865726
申请日：2013-04-18
Applicant: Headwaters Heavy Oil, LLC
Inventor： Roger K. Lott , Lap Keung Lee
IPC: C10G47/06 , C10G47/26 , B01J8/08 , C10G45/16 , C10G45/56 , B01J8/22 , C10G67/08 , C10G65/02 , C10G49/00 , C10G49/12 , C10G45/04 , C10G45/34 , C10G45/46 , C10G65/00
CPC classification number: C10G47/06 , B01J8/08 , B01J8/22 , B01J8/226 , C10G45/04 , C10G45/16 , C10G45/34 , C10G45/46 , C10G45/56 , C10G47/26 , C10G49/005 , C10G49/12 , C10G65/00 , C10G65/02 , C10G67/08 , C10G2300/1033 , C10G2300/107 , C10G2300/1077 , C10G2300/202 , C10G2300/206 , C10G2300/4056 , C10G2300/70 , C10G2300/703 , C10G2300/802
Abstract: A hydrocracking system is upgraded by modifying an existing ebullated bed initially utilizing a supported ebullated bed catalyst to thereafter utilize a dual catalyst system that includes metal sulfide catalyst particles and supported ebullated bed catalyst. The upgraded hydrocracking system achieves at least one of: (1) hydroprocess lower quality heavy oil; (2) increase conversion of higher boiling hydrocarbons that boil at 524° C. (975° F.) or higher; (3) reduce the concentration of supported ebullated bed catalyst required to operate an ebullated bed reactor at a given conversion level; and/or (4) proportionally convert the asphaltene fraction in heavy oil at the same conversion level as the heavy oil as a whole. The metal sulfide catalyst may include colloidal or molecular catalyst particles less than 1 micron in size and formed in situ within the heavy oil using a catalyst precursor well-mixed within the heavy oil and decomposed to form catalyst particles.
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