公开(公告)号：US20240367130A1

公开(公告)日：2024-11-07

申请号：US18651140

申请日：2024-04-30

Applicant: Qatar Foundation for Education, Science and Community Development

Inventor： Konstantinos E. Kakosimos ,  Mohammed Al Hashimi ,  Suhde Mecid Makki ,  Amer Haki ,  Ahmed Abbas ,  Dhabia Al Mohannadi ,  Lina Rueda ,  Santhosh Sukumaran

IPC: B01J8/08

Abstract: A hybrid slurry reactor for performing photocatalytic reactions is provided. The hybrid slurry reactor includes a photoreactor, including a conduit, having a transparent portion, a light-emitting diode (LED) array disposed within the conduit; wherein the conduit is configured such that photons from an external source enter the conduit through the transparent portion and the LED array is directed to emit photons into the conduit.

公开(公告)号：US20240293788A1

公开(公告)日：2024-09-05

申请号：US18565297

申请日：2022-06-09

Applicant: Universiteit Antwerpen

Inventor： Serge Tavernier M.F. ,  Yorick Clauwers ,  Toon Bouwen

IPC: B01J8/10 ,  B01J8/08 ,  C12M1/40

CPC classification number: B01J8/10 ,  B01J8/082 ,  B01J8/085 ,  B01J8/087 ,  C12M21/18 ,  B01J2208/00628

Abstract: The present invention relates to devices for maintaining a state of equilibrium, and process set-ups to perform equilibrium reactions using heterogeneous catalysts, in particular said reactions are equilibrium reactions where at least one reaction product is volatile. The invention is especially interesting for enzymatic reactions using immobilized enzymes, although it is also useful for pure chemical reactions. The invention is characterized by a combination of non-impact mixing of components and volatilization and/or removal of excess molecules, thereby maintaining a state of equilibrium or driving an equilibrium reaction. The present invention also relates to devices and/or process set-ups and materials made using said processes.

公开(公告)号：US20240238747A1

公开(公告)日：2024-07-18

申请号：US18574374

申请日：2022-07-01

Applicant: BEIJING UNIVERSITY OF CHEMICAL TECHNOLOGY

Inventor： Jianfeng CHEN ,  Guangwen CHU ,  Liangliang ZHANG ,  Baochang SUN ,  Haikui ZOU ,  Yong LUO

IPC: B01J8/10 ,  B01J8/08

CPC classification number: B01J8/10 ,  B01J8/087 ,  B01J2208/00132 ,  B01J2208/00867

Abstract: The present invention discloses an immersion type rotating packed-bed reactor and an application thereof. A rotor filler is immersed in materials in the reactor; under the driving of the rotation of a rotor, the materials in the reactor form a loop; and when passing through the filler, the materials are fully sheared and dispersed into fluid micro-elements, so that the mass transfer rate and the reaction rate are increased. A feeding assembly simultaneously introduces materials of different phases to an inner edge of the rotor, a retaining ring and a baffle function to break a vortex, and a heat exchange assembly can maintain a system in a suitable temperature range. The present invention is suitable for heterogeneous systems such as a gas-liquid system and a liquid-liquid system. Compared with a conventional rotating packed bed, the material contact time is long, so that the reaction is more complete.

公开(公告)号：US20240228892A1

公开(公告)日：2024-07-11

申请号：US18563540

申请日：2022-05-20

Applicant: IFP ENERGIES NOUVELLES

Inventor： Ludovic NOEL ,  Christophe PIERRE ,  Sébastien LECARPENTIER ,  Pierre-Yves LE GOFF ,  Victorian GAZEYEFF ,  Matthieu LAFONTAINE

IPC: C10G35/12 ,  B01J8/00 ,  B01J8/08

CPC classification number: C10G35/12 ,  B01J8/0025 ,  B01J8/082 ,  B01J2208/00106 ,  B01J2208/00539 ,  B01J2208/00584 ,  B01J2208/00628 ,  C10G2400/20 ,  C10G2400/22 ,  C10G2400/30

Abstract: The invention relates to a process for the catalytic treatment of a hydrocarbon feedstock with continuous catalytic regeneration, in which process said feedstock is successively circulated in a plurality of reaction zones in series (R1, R2, R3, R4), the catalyst circulating as a moving bed successively in the plurality of reaction zones and flowing from the upstream end to the downstream end of each of the reaction zones and being transported by a carrier gas phase g1 from the downstream end of one reaction zone to the upstream end of the next reaction zone, characterized in that said carrier gas phase g1 has a density of greater than or equal to 1 kg/m3.

公开(公告)号：US20240173685A1

公开(公告)日：2024-05-30

申请号：US18386700

申请日：2023-11-03

Applicant: Sumitomo Chemical Company, Limited

Inventor： Kazuyuki TAKEMURA ,  Tsuyoshi TATSUI ,  Kojiro MATSUI ,  Masahiro MIWA

IPC: B01J8/12 ,  B01J8/08 ,  C08F10/00

CPC classification number: B01J8/12 ,  B01J8/085 ,  C08F10/00 ,  B01J2208/00752 ,  B01J2208/00761 ,  B01J2208/0084

Abstract: An olefin polymerization reactor capable of efficiently removing heat of reaction and having excellent energy saving properties is described. The olefin polymerization reactor includes a tubular powder container forming a moving bed in which powder moves downward by gravity, and including a plurality of intermediate openings provided spaced apart from each other in a vertical direction, a gas container that accommodates gas discharged from the plurality of intermediate openings, a powder feed pipe that feeds, to an upper portion of the tubular powder container, polyolefin powder and/or slurry containing polyolefin powder and olefin monomer liquid, a liquid feed pipe that feeds olefin monomer liquid to an inside of the tubular powder container, and a gas discharge pipe that discharges olefin monomer gas from the gas container to outside.

公开(公告)号：US11865528B2

公开(公告)日：2024-01-09

申请号：US18353149

申请日：2023-07-17

Applicant: Chevron Phillips Chemical Company LP

Inventor： Masud M. Monwar ,  Carlos A. Cruz ,  Jared L. Barr ,  Max P. McDaniel

IPC: C08F110/02 ,  C08F210/16 ,  C08F4/69 ,  B01J31/12 ,  C08F10/02 ,  B01J8/08 ,  B01J8/18 ,  B01J19/12 ,  B01J21/08 ,  C08F4/22 ,  B01J23/26 ,  B01J37/16 ,  C08F4/78 ,  B01J37/34 ,  B01J31/34

CPC classification number: B01J31/12 ,  B01J8/085 ,  B01J8/18 ,  B01J19/123 ,  C08F10/02 ,  C08F110/02 ,  C08F210/16 ,  B01J21/08 ,  B01J23/26 ,  B01J31/34 ,  B01J37/16 ,  B01J37/34 ,  B01J37/344 ,  B01J37/345 ,  B01J2219/089 ,  B01J2219/0869 ,  B01J2219/1203 ,  B01J2531/62 ,  C08F4/22 ,  C08F4/69 ,  C08F4/78

Abstract: Supported chromium catalysts with an average valence less than +6 and having a hydrocarbon-containing or halogenated hydrocarbon-containing ligand attached to at least one bonding site on the chromium are disclosed, as well as ethylene-based polymers with terminal alkane, aromatic, or halogenated hydrocarbon chain ends. Another ethylene polymer characterized by at least 2 wt. % of the polymer having a molecular weight greater than 1,000,000 g/mol and at least 1.5 wt. % of the polymer having a molecular weight less than 1000 g/mol is provided, as well as an ethylene homopolymer with at least 3.5 methyl short chain branches and less than 0.6 butyl short chain branches per 1000 total carbon atoms.

公开(公告)号：US20230416419A1

公开(公告)日：2023-12-28

申请号：US18463380

申请日：2023-09-08

Applicant: Chevron Phillips Chemical Company LP

Inventor： Max P. McDaniel ,  Carlton E. Ash ,  Kathy S. Clear ,  Eric D. Schwerdtfeger ,  Carlos A. Cruz ,  Jeremy M. Praetorius ,  Youlu Yu

IPC: C08F10/02 ,  B01J8/08 ,  B01J19/24 ,  C08K3/08 ,  C08K3/36

CPC classification number: C08F10/02 ,  B01J8/08 ,  B01J19/2455 ,  C08K3/08 ,  C08K3/36

Abstract: Supported chromium catalysts containing a solid oxide and 0.1 to 15 wt. % chromium, in which the solid oxide or the supported chromium catalyst has a particle size span from 0.5 to 1.4, less than 3 wt. % has a particle size greater than 100 μm, and less than 10 wt. % has a particle size less than 10 μm, can be contacted with an olefin monomer in a loop slurry reactor to produce an olefin polymer. Representative ethylene-based polymers produced using the chromium catalysts have a HLMI of 4 to 70 g/10 min, a density from 0.93 to 0.96 g/cm3, from 150 to 680 ppm solid oxide (such as silica), from 1.5 to 6.8 ppm chromium, and a film gel count of less than 15 catalyst particle gels per ft2 of 25 micron thick film and/or a gel count of less than or equal to 50 catalyst particles of greater than 100 μm per five grams of the ethylene polymer.

公开(公告)号：US20230381729A1

公开(公告)日：2023-11-30

申请号：US18199783

申请日：2023-05-19

Applicant: NuMat Tec.comhnologies, Inc

Inventor： Glenn McPherson Tom ,  Nicolaas Vermeulen ,  Anton H. Nguyen ,  Javan L. Whitney-Warner

IPC: B01J8/22 ,  B01D15/18 ,  B01J8/34 ,  B01J8/08 ,  B01J8/38

CPC classification number: B01J8/226 ,  B01D15/1807 ,  B01J8/34 ,  B01J8/085 ,  B01J8/386 ,  B01J2208/00548

Abstract: A spin contactor is provided for contacting a particulate with a fluid. The spin contactor has a containment section that may contain the particulate, a fluid inlet, and a fluid outlet. The containment section comprises an upper particulate separator, a lower particulate separator, and a conical wall. In most cases, the spin contactor includes a shaft to be operatively coupled to a means for spinning the spin contactor. The fluid is drawn upwardly through the fluid inlet to contact the particulate and then expelled through the fluid outlet. A process of treating a fluid composition is provided by sending the fluid composition through the spin contactor comprising particulates.

公开(公告)号：US20230364574A1

公开(公告)日：2023-11-16

申请号：US18027882

申请日：2021-09-21

Applicant: Basell Polyolefine GmbH

Inventor： Tiziana Caputo ,  Pietro Baita ,  Maria Di Diego ,  Lorella Marturano ,  Antonio Mazzucco ,  Gabriele Mei ,  Giulia Mei ,  Roberta Pica

IPC: B01J8/10 ,  B01J8/08 ,  B01J8/00 ,  C08F2/01 ,  C08F4/619 ,  C08F110/02

CPC classification number: B01J8/10 ,  B01J8/085 ,  B01J8/003 ,  C08F2/01 ,  C08F4/61912 ,  C08F110/02 ,  B01J2208/00752 ,  B01J2208/00761

Abstract: An apparatus for polymerizing olefins including a polymerization reactor and a vessel system for pre-activating a solid catalyst component, wherein the vessel system is arranged upstream of the polymerization reactor. The vessel system includes a contacting vessel which includes a main portion, a base portion, a head portion, an inlet, an outlet, and a stirrer positioned within the contacting vessel, wherein the ratio (H/D) of the height (H) of the main portion to the diameter (D) of the main portion is 1.8 or greater. The stirrer is located at a position between the inlet and the outlet.

公开(公告)号：US20230356172A1

公开(公告)日：2023-11-09

申请号：US18323829

申请日：2023-05-25

Applicant: KABUSHIKI KAISHA TOSHIBA ,  TOSHIBA ENERGY SYSTEMS & SOLUTIONS CORPORATION

Inventor： Koji MIZUGUCHI ,  Satoshi MIKOSHIBA ,  Ryota KITAGAWA ,  Takehiko MURAMATSU

IPC: B01J19/00 ,  C25B1/23 ,  C25B15/023 ,  C07C1/12 ,  B01J8/08 ,  C25B15/08

CPC classification number: B01J19/0033 ,  B01J8/082 ,  C07C1/12 ,  C25B1/23 ,  C25B15/023 ,  C25B15/081 ,  B01D53/02

Abstract: A carbon compound manufacturing system includes: a recovery unit; a conversion unit; a synthesis unit; a first flow path to supply the supply gas to the recovery unit; a second flow path connecting the recovery and the conversion units; a third flow path connecting the conversion and the synthesis units; at least one of first to third detectors to respectively measure a flow rate of the supply gas flowing through the first flow path to generate a first data signal, a flow rate of the carbon dioxide flowing through the second flow path to generate a second data signal, and a value of voltage or current to the conversion unit to generate a third data signal; and an integration controller to collate at least one data of the first to third data signals with a corresponding plan data to generate at least one of first to third control signals.