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公开(公告)号:US11772064B2
公开(公告)日:2023-10-03
申请号:US17617149
申请日:2020-03-23
Inventor: Jing Meng , Zhilong Wei , Hui Wei , Yubo Li
CPC classification number: B01J19/1881 , B01J4/001 , B01J19/18 , B01J2203/00 , B01J2204/002 , B01J2204/005
Abstract: A reaction apparatus, comprising: a reaction kettle; a circulation loop, comprising a circulation pipeline and a circulator pump provided on the circulation pipeline, a discharging end of the circulator pump being communicated with the top of the reaction kettle by means of a circulation valve and a charging end of the circulator pump being communicated with the bottom of the reaction kettle by means of a block valve; a feeding loop, comprising a feeding pipeline and a bypass pipeline, the feeding pipeline being provided between the block valve and the circulator pump and being communicated with the circulation pipeline, the bypass pipeline being provided with a control valve, and one end of the bypass pipeline being communicated with the discharging end of the circulator pump and the other end thereof being communicated with the bottom of the reaction kettle; and a discharging loop, comprising a discharging pipeline provided between the circulator pump and the circulation valve and communicated with the circulation pipeline, the discharging pipeline being provided with a discharging valve.
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公开(公告)号:US20230227734A1
公开(公告)日:2023-07-20
申请号:US17894481
申请日:2022-08-24
Inventor: Francis MILLER , Steve ADDLEMAN , Timothy PHILLIPS
IPC: C10G27/14 , B01D17/02 , B01D17/04 , B01D17/12 , B01J4/00 , C10G31/10 , C10G33/04 , E21B43/16 , B01F23/231 , C10G31/08
CPC classification number: C10G27/14 , B01D17/0205 , B01D17/047 , B01D17/12 , B01J4/001 , C10G31/10 , C10G33/04 , E21B43/16 , B01F23/231 , C10G31/08 , C10G2300/1033 , C10G2300/80
Abstract: A method of treating a contaminated oil comprising preparing a brine solution, adding ozone to the brine solution to produce ozonated brine solution, adding a volume of ozonated brine solution to a volume of the contaminated oil, mixing the volumes of contaminated oil and ozonated brine solution with coagulant and surfactant at a shear rate sufficiently high so as to cause formation of an emulsion of the contaminated oil and the brine solution, stopping the mixing, thereby causing the emulsion to separate into an aqueous brine liquid phase and an oil liquid phase, separating the brine liquid phase from the oil liquid phase, and separating at least one contaminant from the oil liquid phase to produce a volume of purified oil.
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公开(公告)号:US11702432B2
公开(公告)日:2023-07-18
申请号:US16979230
申请日:2019-02-13
Applicant: Dow Silicones Corporation
Inventor: Anthony E. Foss , Jesse A. Maddock , Brian D. Rekken , Michael D. Telgenhoff
CPC classification number: C07F7/10 , B01J4/001 , B01J19/0053 , C07F7/025
Abstract: A method of making an aminosilane, the method comprising: forming a reaction mixture comprising a hydridosilane, an amine and a dehydrogenative coupling catalyst in a reactor; subjecting the reaction mixture to conditions sufficient to cause a dehydrogenative coupling reaction between the hydridosilane and the amine to form the aminosilane and hydrogen gas; and venting the hydrogen gas; wherein the forming of the reaction mixture comprising the hydridosilane, the amine and the dehydrogenative coupling catalyst comprises continuously feeding the hydridosilane to the reactor containing the amine and the dehydrogenative coupling catalyst.
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公开(公告)号:US20230211358A1
公开(公告)日:2023-07-06
申请号:US17924061
申请日:2021-05-27
Applicant: Solugen, Inc.
Inventor: Sean T. Hunt , Kenneth Keckler
CPC classification number: B03D1/1431 , B01F23/214 , B01F23/454 , B01F23/808 , B01F25/53 , B01J4/004 , B01J8/002 , B01J8/004 , B03D1/1493 , B01F2101/44
Abstract: A reactor system includes a reactor vessel configured to contain a process fluid, and a sparger assembly that operably coupled to the reactor vessel and configured to supply a mixture of a gas and a recirculated process fluid to the reactor vessel. The sparger assembly includes a plurality of sparger chambers. Each sparger chamber includes a process fluid conduit fluidly coupled to a process fluid return of the reactor vessel via a process fluid inlet, wherein the process fluid inlet has a first block and bleed valve assembly. Each sparger chamber includes a sparger conduit fluidly coupled to the process fluid conduit and a sparger disposed within the sparger conduit and fluidly coupled to a gas source via a gas inlet. Each sparger chamber also includes a process fluid-gas mixture outlet that fluidly couples the sparger conduit to a sparger outlet of the reactor vessel.
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公开(公告)号:US20230203268A1
公开(公告)日:2023-06-29
申请号:US17996012
申请日:2021-04-13
Applicant: Eastman Chemical Company
Inventor: Bruce Roger DeBruin , Michael Paul Ekart , Xianchun Wu , David Eugene Slivensky , Daryl Bitting , Anne-Martine Sherbeck Jackson , Nathan Mitchell West , Zhufang Liu
IPC: C08J11/08 , B01J4/00 , C07C51/38 , C07C29/147
CPC classification number: C08J11/08 , B01J4/001 , C07C51/38 , C07C29/147 , C08J2367/02
Abstract: Chemical recycling facilities for processing mixed waste plastic are provided herein. Such facilities have the capability of processing mixed plastic waste streams and utilize a variety of recycling facilities, such as, for example, solvolysis facility, a pyrolysis facility, a cracker facility, a partial oxidation gasification facility, an energy recovery facility, and a solidification facility. Streams from one or more of these individual facilities may be used as feed to one or more of the other facilities, thereby maximizing recovery of valuable chemical components and minimizing unusable waste streams.
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公开(公告)号:US11679992B2
公开(公告)日:2023-06-20
申请号:US17043623
申请日:2019-06-11
Applicant: Microvast Power Systems Co., LTD.
Inventor: Bryan Yonemoto , Xiao Zhang
IPC: C01G53/00 , B01J4/00 , C01G53/06 , H01M4/04 , H01M4/131 , H01M4/1391 , H01M4/525 , B01J19/00 , H01M4/139 , H01M4/13 , H01M10/0525 , H01M4/02
CPC classification number: C01G53/006 , B01J4/008 , B01J19/0086 , C01G53/06 , H01M4/0497 , H01M4/13 , H01M4/131 , H01M4/139 , H01M4/1391 , H01M4/525 , B01J2204/002 , B01J2219/00177 , B01J2219/00186 , C01P2002/52 , C01P2004/03 , C01P2004/84 , C01P2006/40 , H01M10/0525 , H01M2004/028
Abstract: The invention relates to a method for preparing core-shell structured particle precursor under a co-precipitation reaction. In this method, by controlling the feeding of different types of anion compositions and/or cation compositions, and adjusting the pH to match with the species, precipitated particles are deposited to form a precipitated particle slurry, filtering, and drying the precipitated particle slurry to yield the particle precursor. The invention also provides a particle precursor which includes a core-shell structure. The shell is made of gradient anions and/or cations. Such particle precursor can be used to prepare cathode of lithium-ion battery.
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公开(公告)号:US11648518B2
公开(公告)日:2023-05-16
申请号:US17610289
申请日:2020-06-19
Applicant: Haldor Topsøe A/S
Inventor: Marc Nybo Hammer , Klaus Risbjerg Jarlkov , Rasmus Asker Calundann
CPC classification number: B01J8/0085 , B01J8/0065 , B01J8/0278 , B01J2208/00654 , B01J2208/00752 , B01J2208/00938
Abstract: A catalytic reactor comprises a floating particle catcher unit and a particle catching surface which extracts particles from the fluid flow stream above the catalyst bed whereby at least a part of the particles settles on the particle catching surface instead of clogging the catalyst bed.
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公开(公告)号:US20230144856A1
公开(公告)日:2023-05-11
申请号:US17911159
申请日:2021-03-12
Applicant: UNIVERSITY OF MARYLAND, COLLEGE PARK
Inventor: Dongxia LIU , Yonggang YAO , Liangbing HU , Qi DONG
IPC: B01J15/00 , B01J19/00 , B01J19/24 , B01J6/00 , B01J4/00 , C01C1/04 , C01B3/26 , C08J7/12 , B29C71/02 , C10G15/08 , C10G50/00
CPC classification number: B01J15/005 , B01J4/008 , B01J6/008 , B01J19/0013 , B01J19/2475 , C01B3/26 , C01C1/0417 , C01C1/0452 , C08J7/08 , C08J7/12 , C10G15/08 , C10G50/00 , B01J2204/005 , B01J2219/00058 , B01J2219/00135 , C01B2203/085 , C01B2203/0277 , C01B2203/1241
Abstract: One or more reactants are flowed into thermal contact with a heating element in a reactor for a first time period. During a first part of a heating cycle, the one or more reactants are provided with a first temperature by heating with the heating element, such that one or more thermochemical reactions is initiated. The one or more thermochemical reactions includes pyrolysis, thermolysis, synthesis, hydrogenation, dehydrogenation, hydrogenolysis, or any combination thereof. The first heating element operates by Joule heating and has a porous construction that allows gas to flow therethrough. During a second part of the heating cycle, the one or more reactants are provided with a second temperature less than the first temperature, for example, by de-energizing the heating element. A duration of the first time period is equal to or greater than a duration of the heating cycle, which is less than five seconds.
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公开(公告)号:US20230123390A1
公开(公告)日:2023-04-20
申请号:US18081732
申请日:2022-12-15
Applicant: SABIC Global Technologies B.V.
Abstract: In an embodiment, a reactor for carrying out a melt transesterification reaction at a reactor temperature of 160 to 300° C. and a reactor pressure of 5 to 200 mbar, comprises a cylindrical tank comprising a top, a side, and a bottom, wherein the bottom is convex, extending away from the top; a stirring shaft disposed within the cylindrical tank along an axis thereof so that it is rotatable from outside of the cylindrical tank; a stirring blade extending from the stirring shaft in the cylindrical tank; a reactant solution inlet located on the bottom; and a reaction solution outlet located on the bottom. The reactor can be used for the polymerization of a polycarbonate oligomer.
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公开(公告)号:US11623900B2
公开(公告)日:2023-04-11
申请号:US17166214
申请日:2021-02-03
Applicant: Chevron Phillips Chemical Company LP
Inventor: Bruce E. Kreischer
IPC: C07C2/08 , B01J8/10 , B01J19/18 , B01J19/24 , C07C2/32 , C07C2/88 , C07C2/30 , B01J8/22 , B01J4/00 , B01J4/02
Abstract: A process includes periodically or continuously introducing an olefin monomer and periodically or continuously introducing a catalyst system or catalyst system components into a reaction mixture within a reaction system, oligomerizing the olefin monomer within the reaction mixture to form an oligomer product, and periodically or continuously discharging a reaction system effluent comprising the oligomer product from the reaction system. The reaction system includes a total reaction mixture volume and a heat exchanged portion of the reaction system comprising a heat exchanged reaction mixture volume and a total heat exchanged surface area providing indirect contact between the reaction mixture and a heat exchange medium. A ratio of the total heat exchanged surface area to the total reaction mixture volume within the reaction system is in a range from 0.75 in−1 to 5 in−1, and an oligomer product discharge rate from the reaction system is between 1.0 (lb)(hr−1)(gal−1) to 6.0 (lb)(hr−1)(gal−1).
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