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公开(公告)号:US11745170B2
公开(公告)日:2023-09-05
申请号:US17232359
申请日:2021-04-16
Applicant: Saudi Arabian Oil Company
Inventor: Lianhui Ding , Manal Al-Eid
IPC: B01J29/06 , B01J29/70 , B01J23/883 , B01J37/04 , B01J35/00 , B01J37/08 , B01J29/12 , B01J29/064 , B01J29/14 , B01J29/10 , B01J29/076 , B01J29/72 , B01J29/76 , B01J29/74 , B01J29/16 , B01J29/80 , B01J35/10 , C01B39/46 , C01B39/02 , B01J37/10 , B01J37/02 , C01B39/52 , C01B39/48 , B01J23/42 , C10G11/05
CPC classification number: B01J29/70 , B01J23/883 , B01J29/06 , B01J29/061 , B01J29/064 , B01J29/076 , B01J29/106 , B01J29/126 , B01J29/146 , B01J29/166 , B01J29/72 , B01J29/74 , B01J29/76 , B01J29/80 , B01J35/006 , B01J35/0006 , B01J35/0046 , B01J35/109 , B01J35/1057 , B01J35/1061 , B01J37/0201 , B01J37/04 , B01J37/08 , B01J37/10 , C01B39/02 , C01B39/46 , C01B39/48 , C01B39/52 , B01J23/42 , B01J2029/062 , B01J2229/18 , B01J2229/183 , B01J2229/186 , B01J2229/42 , C10G11/05
Abstract: Embodiments of the present disclosure are directed to hydrocracking catalysts and methods of making same. The hydrocracking catalyst comprises a platinum encapsulated zeolite having a crystallinity greater than 20% determined by X-ray powder diffraction analysis.
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公开(公告)号:US20230271172A1
公开(公告)日:2023-08-31
申请号:US18303556
申请日:2023-04-19
Applicant: Mississippi State University
Inventor: Mark G. White , Shetian Liu
IPC: B01J29/78 , B01J29/08 , B01J23/28 , C10L3/12 , C10L1/08 , C10G2/00 , B01J37/02 , B01J29/48 , B01J29/16 , B01J29/076
CPC classification number: B01J29/7815 , B01J29/78 , B01J29/084 , B01J23/28 , C10L3/12 , C10L1/08 , C10G2/334 , B01J37/0201 , B01J29/48 , B01J29/166 , B01J29/076 , B01J2229/18 , B01J29/7876 , B01J29/26
Abstract: The present invention provides a novel process and system in which a mixture of carbon monoxide and hydrogen synthesis gas, or syngas, is converted into hydrocarbon mixtures composed of high quality gasoline components, aromatic compounds, and lower molecular weight gaseous olefins in one reactor or step. The invention utilizes a novel molybdenum-zeolite catalyst in high pressure hydrogen for conversion, as well as a novel rhenium-zeolite catalyst in place of the molybdenum-zeolite catalyst, and provides for use of the novel catalysts in the process and system of the invention.
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公开(公告)号:US20230271161A1
公开(公告)日:2023-08-31
申请号:US17892924
申请日:2022-08-22
Applicant: Sasol Germany GmbH
Inventor: Marcos Schoneborn , Noelia Guillen-Hurtado , Thomas Harmening , Dirk Niemeyer , Diane Howe
IPC: B01J23/00 , B01J35/10 , F01N3/28 , B01J23/10 , B01J37/00 , B01J37/02 , B01J35/00 , C04B41/50 , B01J37/03 , C04B41/00 , C04B41/87 , F01N13/16 , B01J21/04
CPC classification number: B01J23/002 , B01J35/1061 , F01N3/2828 , B01J23/10 , B01J35/1042 , B01J37/0045 , B01J37/0203 , B01J35/1023 , B01J35/1014 , B01J35/1038 , B01J35/1019 , B01J35/1085 , B01J35/002 , C04B41/5045 , B01J37/035 , C04B41/009 , C04B41/87 , B01J37/0236 , B01J37/0201 , F01N13/16 , B01J21/04 , C04B2235/3217 , C04B2235/3224 , F01N2510/063 , B01J35/008 , B01J2523/00 , C04B2235/44 , F01N3/101
Abstract: The present invention relates to a metal oxide coated composite comprising a core consisting of a mixture of a La stabilized Al2O3 phase and an Ce/Zr/RE2O3 mixed oxide phase, the core having a specific crystallinity, specific pore volume and a specific pore size distribution, and a method for the production of the metal oxide coated composite.
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公开(公告)号:US20230256414A1
公开(公告)日:2023-08-17
申请号:US18011540
申请日:2021-06-25
Applicant: BASF SE
Inventor: Sung Yeun CHOI , Andrey KARPOV , Christian WALSDORFF , Patrick HUBACH , Karl KHARAS
CPC classification number: B01J21/04 , B01J35/1042 , B01J35/1047 , B01J23/50 , B01J6/001 , B01J37/0201 , C07C29/50
Abstract: A process for producing a porous alpha-alumina catalyst support, comprising i) preparing a precursor material comprising, based on inorganic solids content, at least 50 wt.-% of a transition alumina having a loose bulk density of at most 600 g/L, a pore volume of at least 0.6 mL/g and a median pore diameter of at least 15 nm; and at most 30 wt.-% of an alumina hydrate; ii) forming the precursor material into shaped bodies; and iii) calcining the shaped bodies to obtain the porous alpha-alumina catalyst support. The catalyst support has a high overall pore volume, thus allowing for impregnation with a high amount of silver, while keeping its surface area sufficiently large so as to provide optimal dispersion of catalytically active species, in particular metal species. The invention further relates to a shaped catalyst body for producing ethylene oxide by gas-phase oxidation of ethylene, comprising at least 15 wt.-% of silver, relative to the total weight of the catalyst, deposited on a porous alpha-alumina catalyst support obtained in the process described above. The invention also relates to a process for preparing a shaped catalyst body as described above comprising impregnating a porous alpha-alumina catalyst support obtained in the process described above with a silver impregnation solution, preferably under reduced pressure; and optionally subjecting the impregnated porous alumina support to drying; and b) subjecting the impregnated porous alpha-alumina support to a heat treatment; wherein steps a) and b) are optionally repeated. The invention further relates to a process for producing ethylene oxide by gas-phase oxidation of ethylene, comprising reacting ethylene and oxygen in the presence of a shaped catalyst body as described above.
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公开(公告)号:US11713705B2
公开(公告)日:2023-08-01
申请号:US17483135
申请日:2021-09-23
Applicant: BASF Corporation
Inventor: Yuejin Li , Xiaolai Zheng , Stanley Roth , Olga Gerlach , Andreas Sundermann
IPC: B01J23/10 , B01J23/44 , B01J23/46 , B01J23/52 , B01J23/63 , B01J33/00 , B01J35/00 , B01J35/04 , B01J35/10 , B01J37/02 , B01J37/08 , F01N3/08 , F01N3/10 , F01N3/20 , F01N3/28 , B01D53/94 , B01J23/42 , B01J35/02
CPC classification number: F01N3/2066 , B01D53/9427 , B01J23/10 , B01J23/42 , B01J23/44 , B01J23/464 , B01J23/468 , B01J23/52 , B01J23/63 , B01J33/00 , B01J35/0006 , B01J35/04 , B01J35/1014 , B01J35/1019 , B01J35/1038 , B01J37/0201 , B01J37/0215 , B01J37/0244 , B01J37/0246 , B01J37/0248 , B01J37/08 , B01J37/082 , B01J37/088 , F01N3/0842 , F01N3/101 , F01N3/2839 , B01D53/945 , B01D53/9468 , B01D53/9472 , B01D2255/1025 , B01D2255/2065 , B01D2255/9022 , B01D2255/9032 , B01D2255/9155 , B01D2255/9205 , B01D2255/9207 , B01D2257/402 , B01J35/006 , B01J35/023 , B01J2523/00 , Y02C20/10 , Y02T10/12 , B01J2523/00 , B01J2523/36 , B01J2523/3712 , B01J2523/822 , B01J2523/00 , B01J2523/3706 , B01J2523/3712 , B01J2523/822 , B01J2523/00 , B01J2523/3712 , B01J2523/3718 , B01J2523/822 , B01J2523/00 , B01J2523/3712 , B01J2523/3725 , B01J2523/822 , B01J2523/00 , B01J2523/3712 , B01J2523/3737 , B01J2523/822 , B01J2523/00 , B01J2523/3712 , B01J2523/375 , B01J2523/822
Abstract: A nitrous oxide (N2O) removal catalyst composite is provided, comprising a N2O removal catalytic material on a substrate, the catalytic material comprising a rhodium (Rh) component supported on a ceria-based support, wherein the catalyst composite has a H2-consumption peak of about 100° C. or less as measured by hydrogen temperature-programmed reduction (H2-TPR). Methods of making and using the same are also provided.
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公开(公告)号:US11713424B2
公开(公告)日:2023-08-01
申请号:US15896507
申请日:2018-02-14
Applicant: Chevron Phillips Chemical Company LP
Inventor: Ryan W. Snell , Scott G. Morrison , Vincent D. McGahee , Xianghong Hao , Gabriela Alvez-Manoli
IPC: C10G61/00 , C10G61/06 , C10G35/04 , C10G45/02 , C10G69/08 , B01D53/14 , C10G59/02 , B01J29/62 , B01J37/02 , C10G61/02
CPC classification number: C10G61/06 , B01D53/1468 , B01J29/62 , B01J37/0201 , C10G35/04 , C10G45/02 , C10G59/02 , C10G61/02 , C10G69/08 , B01D2257/304 , C10G2300/202 , C10G2300/207 , C10G2300/4006 , C10G2300/4031 , C10G2300/70 , C10G2300/701 , C10G2400/30
Abstract: A process for operating a reforming system by operating a reforming section containing a plurality of reactors, wherein each of the plurality of reactors containing a reforming catalyst capable of catalyzing the conversion of at least a portion of the hydrocarbons in a treated hydrocarbon stream into a reactor effluent comprising aromatic hydrocarbons, and operating a sulfur guard bed (SGB) to remove sulfur and sulfur-containing hydrocarbons from a hydrocarbon feed to provide the treated hydrocarbon stream, where the SGB contains at least a layer of a SGB catalyst comprising the same catalyst as the reforming catalyst, and where each reactor of the plurality of reactors within the reforming section may be operated at a higher operating temperature than an operating temperature of the SGB. A system for carrying out the process is also provided.
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37.
公开(公告)号:US20230219822A1
公开(公告)日:2023-07-13
申请号:US17996054
申请日:2021-04-06
Applicant: N.E. CHEMCAT CORPORATION
Inventor: Yukio TAKAGI , Yasuyuki BANNO , Kiyohiko SAITO , Hiroyasu SUZUKA , Yosuke IMANAKA , Takahiko ISHIKAWA
CPC classification number: C01B39/46 , B01J29/06 , B01J37/0201 , B01J29/7015 , B01J29/7003 , B01D53/86 , C01P2006/16 , B01D2255/50 , B01D2255/9205
Abstract: A small-pore zeolite that is modified with phosphorus, is excellent in hydrothermal durability, and has an 8-membered oxygen ring structure. The 8-membered oxygen ring structure is CHA, AEI, and AFX. The small-pore zeolite incudes at least an aluminum element, a silica element, a phosphorus element, wherein the phosphorus element is defined by expression (1), and the small-pore zeolite has an 8-membered oxygen ring structure being of CHA, AEI, or AFX. The phosphorus element that modifies the zeolite is unevenly distributed and richly contained on the surface layer side of the zeolite. A method for producing a phosphorus element-containing zeolite.
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公开(公告)号:US11680211B2
公开(公告)日:2023-06-20
申请号:US16698468
申请日:2019-11-27
Applicant: FURUKAWA ELECTRIC CO., LTD.
Inventor: Takao Masuda , Yuta Nakasaka , Takuya Yoshikawa , Sadahiro Kato , Masayuki Fukushima , Hiroko Takahashi , Yuichiro Banba , Kaori Sekine
CPC classification number: C10G45/12 , B01J6/001 , B01J29/40 , B01J35/023 , B01J35/1057 , B01J35/1061 , B01J35/1066 , B01J37/0201
Abstract: Provided is a structured catalyst for hydrodesulfurization that suppresses the decline in catalytic activity and achieves efficient hydrodesulfurization. The structured catalyst for hydrodesulfurization (1) includes a support (10) of a porous structure composed of a zeolite-type compound, and at least one catalytic substance (20) present in the support (10), the support (10) having channels (11) connecting with each other, and the catalytic substance (20) being present at least in the channels (11) of the support (10).
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公开(公告)号:US11648538B2
公开(公告)日:2023-05-16
申请号:US16698670
申请日:2019-11-27
Inventor: Takao Masuda , Yuta Nakasaka , Takuya Yoshikawa , Sadahiro Kato , Masayuki Fukushima , Kojiro Inamori , Hiroko Takahashi , Yuichiro Banba , Kaori Sekine
IPC: B01J29/06 , B01J29/14 , B01J29/46 , B01J29/68 , B01J29/76 , B01J35/00 , B01J37/00 , B01J37/02 , B01J37/10 , B01J37/18 , B01J29/064 , B01J29/035 , B01J29/068 , B01J29/076 , B01J29/22 , B01J29/16 , B01J29/18 , B01J29/072 , B01J29/08 , B01J29/20 , B01J29/10 , B01J29/12 , B01J29/62 , B01J29/48 , B01J29/60 , B01J29/44 , B01J29/24 , B01J29/61 , B01J29/26 , B01J29/42 , B01J29/40 , B01J29/69 , B01J29/63 , B01J29/70 , B01J29/65 , B01J29/67 , B01J29/66 , B01J29/64 , B01J29/74 , B01J29/78 , B01J29/72 , B01J35/02 , F01N3/28 , C01B39/02 , B01D53/94
CPC classification number: B01J29/14 , B01D53/94 , B01D53/9409 , B01D53/9413 , B01J29/035 , B01J29/0352 , B01J29/0354 , B01J29/0356 , B01J29/0358 , B01J29/064 , B01J29/068 , B01J29/072 , B01J29/076 , B01J29/085 , B01J29/10 , B01J29/12 , B01J29/16 , B01J29/185 , B01J29/20 , B01J29/22 , B01J29/24 , B01J29/26 , B01J29/40 , B01J29/405 , B01J29/42 , B01J29/44 , B01J29/46 , B01J29/48 , B01J29/605 , B01J29/61 , B01J29/62 , B01J29/63 , B01J29/64 , B01J29/655 , B01J29/66 , B01J29/67 , B01J29/68 , B01J29/69 , B01J29/7007 , B01J29/7038 , B01J29/7049 , B01J29/7057 , B01J29/7088 , B01J29/7215 , B01J29/7276 , B01J29/7415 , B01J29/7476 , B01J29/76 , B01J29/7615 , B01J29/7669 , B01J29/7676 , B01J29/7815 , B01J29/7876 , B01J35/0006 , B01J35/006 , B01J35/0013 , B01J35/0046 , B01J35/0066 , B01J35/0073 , B01J35/023 , B01J35/026 , B01J37/0018 , B01J37/0072 , B01J37/0201 , B01J37/0203 , B01J37/0205 , B01J37/0207 , B01J37/0211 , B01J37/0236 , B01J37/10 , B01J37/105 , B01J37/18 , C01B39/02 , F01N3/2828 , B01D2255/2042 , B01D2255/2063 , B01D2255/2073 , B01D2255/2092 , B01D2255/402 , B01D2255/9155 , B01J2229/126 , B01J2229/14 , B01J2229/186 , B01J2229/20 , B01J2229/22 , B01J2229/32 , B01J2229/34 , B01J2229/38 , B01J2229/40 , C10G2300/70 , F01N2330/06 , F01N2370/04 , F01N2510/063
Abstract: A functional structural body includes a skeletal body of a porous structure composed of a zeolite-type compound, and at least one type of metallic nanoparticles present in the skeletal body, the skeletal body having channels connecting with each other, the metallic nanoparticles being present at least in the channels of the skeletal body.
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40.
公开(公告)号:US20190210008A1
公开(公告)日:2019-07-11
申请号:US16323745
申请日:2017-08-08
Applicant: Tokyo Institute of Technology , Tsubame BHB Co., Ltd.
Inventor: Hideo Hosono , Masaaki Kitano , Toshiharu Yokoyama , Jiang Li , Shigeki Kawamura , Kazuhisa Kishida
CPC classification number: B01J23/58 , B01J21/04 , B01J23/462 , B01J35/10 , B01J35/1009 , B01J37/0201 , B01J37/08 , B01J37/18 , C01C1/04 , C01C1/0411 , Y02P20/52
Abstract: Provided is a method for manufacturing a catalyst with which it is possible to obtain a supported metal ammonia synthesis catalyst, in which there are restrictions in terms of producing method and producing facility, and particularly large restrictions for industrial-scale producing, in a more simple manner and so that the obtained catalyst has a high activity. This method for manufacturing an ammonia synthesis catalyst includes: a first step for preparing 12CaO.7Al2O3 having a specific surface area of 5 m2/g or above; a second step for supporting a ruthenium compound on the 12CaO.7Al2O3; and a third step for performing a reduction process on the 12CaO.7Al2O3 supporting the ruthenium compound, obtained in the second step. This invention is characterized in that the reduction process is performed until the average particle diameter of the ruthenium after the reduction process has increased by at least 15% in relation to the average particle diameter of the ruthenium before the reduction process.
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