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公开(公告)号:US12053761B2
公开(公告)日:2024-08-06
申请号:US18449765
申请日:2023-08-15
Applicant: Chevron Phillips Chemical Company LP
Inventor: Max P. McDaniel , Kathy S. Clear
IPC: B01J23/26 , B01J21/12 , B01J27/047 , B01J27/188 , B01J35/02 , B01J35/10 , B01J35/40 , B01J35/61 , B01J35/63 , B01J37/00 , B01J37/02 , B01J37/08 , B01J37/12 , C08F2/00 , C08F4/78 , C08F110/02
CPC classification number: B01J23/26 , B01J21/12 , B01J27/047 , B01J27/188 , B01J35/40 , B01J35/615 , B01J35/635 , B01J35/638 , B01J37/0045 , B01J37/0209 , B01J37/082 , B01J37/12 , C08F2/00 , C08F4/78 , C08F110/02 , C08F110/02 , C08F2500/04 , C08F2500/12
Abstract: Methods for making a supported chromium catalyst are disclosed, and can comprise contacting a silica-coated alumina containing at least 30 wt. % silica with a chromium-containing compound in a liquid, drying, and calcining in an oxidizing atmosphere at a peak temperature of at least 650° C. to form the supported chromium catalyst. The supported chromium catalyst can contain from 0.01 to 20 wt. % chromium, and typically can have a pore volume from 0.5 to 2 mL/g and a BET surface area from 275 to 550 m2/g. The supported chromium catalyst subsequently can be used to polymerize olefins to produce, for example, ethylene-based homopolymers and copolymers having high molecular weights and broad molecular weight distributions.
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公开(公告)号:US11986813B2
公开(公告)日:2024-05-21
申请号:US17707115
申请日:2022-03-29
Applicant: ALBEMARLE CATALYSTS COMPANY B. V.
Inventor: Marcel Adriaan Jansen , Henk Jan Tromp , Bob Gerardus Oogjen , Sander Hendrikus Lambertus Thoonen , Jan Nieman , Wilhelmus Clemens Jozef Veerman
IPC: B01J37/00 , B01J21/02 , B01J23/85 , B01J23/882 , B01J23/883 , B01J27/188 , B01J35/61 , B01J35/63 , B01J35/64 , B01J37/02 , B01J37/20 , C10G45/08
CPC classification number: B01J37/0009 , B01J21/02 , B01J23/85 , B01J23/882 , B01J23/883 , B01J27/188 , B01J35/613 , B01J35/615 , B01J35/633 , B01J35/635 , B01J35/638 , B01J35/647 , B01J37/0203 , B01J37/0207 , B01J37/0219 , C10G45/08 , B01J37/20 , C10G2300/70
Abstract: A catalyst having at least one Group VIB metal component, at least one Group VIII metal component, a phosphorus component, and a boron-containing carrier component. The amount of the phosphorus component is at least 1 wt %, expressed as an oxide (P2O5) and based on the total weight of the catalyst, and the amount of boron content is in the range of about 1 to about 13 wt %, expressed as an oxide (B2O3) and based on the total weight of the catalyst. In one embodiment of the invention, the boron-containing carrier component is a product of a co-extrusion of at least a carrier and a boron source. A method for producing the catalyst and its use for hydrotreating a hydrocarbon feed are also described.
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公开(公告)号:US20240359167A1
公开(公告)日:2024-10-31
申请号:US18572000
申请日:2021-07-29
Applicant: Toyo Tire Corporation
Inventor: Norihiko Nakamura , Noritatsu Tsubaki , Guohui Yang
CPC classification number: B01J29/405 , B01J35/633 , B01J35/635 , B01J35/638 , B01J35/695 , B01J37/0018 , B01J37/10 , C07C1/24 , C07C2521/06 , C07C2521/08 , C07C2523/06
Abstract: A catalyst according to an embodiment is a catalyst for synthesizing 1,3 -butadiene from ethanol. The catalyst contains a porous silica support made of crystalline silica, Zn, and Zr, and has a multimodal pore size distribution with a peak pore size (Dmicro) of 2 in or less and a peak pore size (Dmeso+macro) of more than 2 nm.
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公开(公告)号:US12048915B2
公开(公告)日:2024-07-30
申请号:US17587723
申请日:2022-01-28
Applicant: Ecovyst Catalyst Technologies LLC
Inventor: Parag Rasiklal Shah , Yatao Rachel Hu
IPC: B01J23/20 , B01J21/08 , B01J35/30 , B01J35/40 , B01J35/61 , B01J35/63 , B01J37/02 , B01J37/04 , B01J37/08 , C07C1/24
CPC classification number: B01J23/20 , B01J21/08 , B01J35/397 , B01J35/40 , B01J35/615 , B01J35/635 , B01J35/638 , B01J37/0207 , B01J37/04 , B01J37/082 , C07C1/24 , C07C2521/08 , C07C2523/20
Abstract: A method for making a supported tantalum oxide catalyst precursor or catalyst with controlled Ta distribution and the resulting supported Ta catalyst. In an embodiment, the method comprises selecting a Ta-precursor with appropriate reactivity with the surface hydroxyls of the solid oxide support material to give a desired Ta distribution in the catalyst precursor or catalyst. In an embodiment the method comprises controlling the number of surface hydroxyls available on the support material to react with the Ta-precursor by thermal methods, such as calcination, to achieve the desired Ta distribution.
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公开(公告)号:US20240207822A1
公开(公告)日:2024-06-27
申请号:US18545922
申请日:2023-12-19
Inventor: Solange Assunção QUINTELLA , Jose Andre Cavalcanti Da Silva , Francisco Murilo Tavares De Luna , Charles Lima Bessa Assuncao , Maria Thiciane Almeida Costa , Celio Loreiro Cavalcante, JR. , Maria Imaculada G. Silveira Teixeira
IPC: B01J23/20 , B01J21/08 , B01J35/30 , B01J35/45 , B01J35/61 , B01J35/63 , B01J35/64 , B01J37/00 , B01J37/02 , B01J37/03 , B01J37/04 , B01J37/08 , C07C67/26 , C10M105/34 , C10N20/00 , C10N20/02
CPC classification number: B01J23/20 , B01J21/08 , B01J35/394 , B01J35/45 , B01J35/617 , B01J35/635 , B01J35/638 , B01J35/647 , B01J37/009 , B01J37/0236 , B01J37/038 , B01J37/04 , B01J37/088 , C07C67/26 , C10M105/34 , C10M2207/2815 , C10N2020/02 , C10N2020/081
Abstract: The present invention relates to a multifunctional hybrid catalyst with niobium and tin supported on hexagonal mesoporous silicas (HMSNb—Sn), synthesis process thereof through isomorphic substitutions and the process for obtaining biodegradable lubricating base oils using said catalyst.
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公开(公告)号:US12036532B2
公开(公告)日:2024-07-16
申请号:US17614913
申请日:2020-05-12
Applicant: MITSUI MINING & SMELTING CO., LTD.
Inventor: Hiroki Tanaka
CPC classification number: B01J23/44 , B01J23/464 , B01J35/19 , B01J35/633 , B01J35/635 , B01J35/638 , B01J37/038 , F01N3/101 , F01N2570/10 , F01N2570/12 , F01N2570/14
Abstract: An exhaust gas purification catalyst comprises a substrate and a catalyst layer on the substrate, and has a first section upstream along a flow direction of the exhaust gas and a second section downstream from the first section. The catalyst layer in the first section comprises a first catalyst layer comprising palladium and a second catalyst layer comprising rhodium and covering the first catalyst layer. A pore volume proportion, which is a proportion of a total volume of the pores having a pore diameter of 0.06-30.0 μm as measured by mercury press-in method and existing in the substrate and the catalyst layer in the first section to a volume of a entire first section, is 12-18%. A wash coat amount, which is a mass per unit volume of the catalyst layer in the first section to the volume of the substrate existing in the first section, is 100-190 g/L.
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公开(公告)号:US20240216896A1
公开(公告)日:2024-07-04
申请号:US18286642
申请日:2022-04-15
Applicant: IFP Energies nouvelles
Inventor: Antoine FECANT , Etienne GIRARD , Philibert LEFLAIVE
IPC: B01J23/887 , B01J35/61 , B01J35/63 , C10G45/08 , C10G45/22
CPC classification number: B01J23/8872 , B01J35/613 , B01J35/615 , B01J35/635 , B01J35/638 , C10G45/08 , C10G45/22 , C10G2300/10 , C10G2300/70 , C10G2400/02
Abstract: Catalyst comprising an active phase based on at least one group VIB metal, at least one group VIII metal, phosphorus, sodium and an alumina-based support, the sodium content being between 50 and 2000 ppm by weight in the form of Na—O relative to the total weight of said catalyst, and the molar ratio of phosphorus to sodium being between 1.5 and 300.
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公开(公告)号:US12017207B2
公开(公告)日:2024-06-25
申请号:US18059712
申请日:2022-11-29
Applicant: Saudi Arabian Oil Company
Inventor: Lianhui Ding , Khalid Otaibi , Faisal Alotaibi
IPC: B01J29/70 , B01J35/23 , B01J35/61 , B01J35/63 , B01J35/64 , B01J37/00 , B01J37/02 , B01J37/03 , B01J37/04 , B01J37/06 , C01B39/48
CPC classification number: B01J29/7007 , B01J35/23 , B01J35/615 , B01J35/617 , B01J35/635 , B01J35/638 , B01J35/647 , B01J37/0018 , B01J37/0236 , B01J37/03 , B01J37/04 , B01J37/06 , C01B39/48 , C01P2004/03 , C01P2004/64 , C01P2006/12 , C01P2006/14 , C01P2006/16
Abstract: Methods for synthesizing a mesoporous nano-sized zeolite beta are described. The method may include mixing an aqueous base solution with hexadecyltrimethylammonium bromide (CTAB) to form a first solution; adding nano-sized zeolite particles having a particle size of less than or equal to 100 nm to the first solution to form a second solution. The nano-sized zeolite particles include a microporous framework with a plurality of micropores having diameters of less than or equal to 2 nm and a BEA framework type. The method may further include transferring the second solution to an autoclave operated at 25° C. to 200° C. for 3 to 24 hours to form a colloid; drying the colloid at 100° C. to 200° C. for 8 to 36 hours without washing the colloid to form a zeolite precursor; and calcining the zeolite precursor at 250° C. to 600° C. for 1 to 8 hours to form the mesoporous nano-sized zeolite beta.
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公开(公告)号:US20240359156A1
公开(公告)日:2024-10-31
申请号:US18691984
申请日:2022-08-26
Inventor: Allen W. Burton , Hilda B. Vroman
CPC classification number: B01J20/18 , B01J20/3057 , B01J29/70 , B01J35/615 , B01J35/638
Abstract: Aluminosilicate zeolites, designated as EMM-63, characterized by a unique powder XRD pattern or unique connectivities, methods of making the same, and uses thereof.
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公开(公告)号:US20240278214A1
公开(公告)日:2024-08-22
申请号:US18568885
申请日:2022-01-18
Applicant: ORGANO CORPORATION
Inventor: Ayumu KATO , Shinji NAKAMURA , Hitoshi TAKADA , Hironao SAJIKI , Tsuyoshi YAMADA , Kwihwan PARK , Yutaro YAMADA
CPC classification number: B01J23/40 , B01J31/08 , B01J35/45 , B01J35/56 , B01J35/635 , B01J35/638 , B01J35/657 , B01J2231/60 , B01J2235/30
Abstract: A method of catalytic hydrogenation and reduction in which a reactive substrate and a hydrogen source are brought into contact in the presence of a platinum-group metal-supported catalyst to run the reactive substrate through catalytic hydrogenation and reduction; the ion exchanger is made of a continuous skeleton phase and a continuous hole phase; the thickness of the continuous skeleton is in the range of 1-100 μm; the average diameter of the continuous holes is in the range of 1-1000 μm; the total pore volume is in the range of 0.5-50 mL/g; the ion exchange capacity per unit weight in a dry state is in the range of 1-9 mg eq/g; and the ion exchanger is a non-particulate, weakly basic, organic porous ion exchanger where an ion exchange group is distributed in the ion exchanger.
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