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1.
公开(公告)号:US20240326032A1
公开(公告)日:2024-10-03
申请号:US18576257
申请日:2022-07-12
Applicant: IFP ENERGIES NOUVELLES
Inventor: Malika BOUALLEG , Laetitia JOTHIE
IPC: B01J37/02 , B01J21/04 , B01J23/755 , B01J35/30 , B01J37/00 , B01J37/08 , B01J37/18 , C07C5/05 , C07C5/11
CPC classification number: B01J37/0205 , B01J21/04 , B01J23/755 , B01J35/393 , B01J35/394 , B01J37/0018 , B01J37/0203 , B01J37/0207 , B01J37/0213 , B01J37/0236 , B01J37/024 , B01J37/088 , B01J37/18 , C07C5/05 , C07C5/11 , C07C2521/04 , C07C2523/755
Abstract: Process for preparing a catalyst comprising a nickel active phase and an alumina support, said catalyst comprising between 1% and 50% by weight of elemental nickel relative to the total weight of the catalyst, the nickel being distributed both over a crust at the periphery of the support, and at the core of the support, which process comprises the following steps:
a) said support is impregnated with a volume V1 of a heptanol solution of between 0.2 and 0.8 times the total pore volume TPV of said support in order to obtain an impregnated support;
b) the impregnated support obtained at the end of step a) is impregnated with a solution comprising a precursor of the nickel active phase in order to obtain a catalyst precursor;
c) the catalyst precursor obtained at the end of step b) is dried at a temperature below 250° C.-
公开(公告)号:US20240299910A1
公开(公告)日:2024-09-12
申请号:US18654882
申请日:2024-05-03
Applicant: Chevron Phillips Chemical Company LP
Inventor: Max P. McDaniel , Kathy S. Clear , Eric D. Schwerdtfeger , Jeremy M. Praetorius
CPC classification number: B01J21/08 , B01J23/26 , B01J37/0217 , B01J37/0236 , B01J37/024 , B01J37/08
Abstract: A method of preparing a catalyst comprising a) drying a chrominated-silica support followed by contacting with a titanium(IV) alkoxide to form a metalized support, b) drying a metalized support followed by contacting with an aqueous alkaline solution comprising from about 3 wt. % to about 20 wt. % of a nitrogen-containing compound to form a hydrolyzed metalized support, and c) drying the hydrolyzed metalized support followed by calcination at a temperature in a range of from about 400° C. to about 1000° C. and maintaining the temperature in the range of from about 400° C. to about 1000° C. for a time period of from about 1 minute to about 24 hours to form the catalyst.
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公开(公告)号:US20240043754A1
公开(公告)日:2024-02-08
申请号:US18266186
申请日:2021-12-09
Applicant: Calor Gas Limited
Inventor: Keith Simons , Hendrick Van Rensburg
CPC classification number: C10G3/49 , B01J29/40 , B01J29/7038 , B01J37/28 , B01J38/12 , B01J35/1019 , B01J35/1038 , B01J35/1061 , B01J37/024 , B01J37/0201 , C10G3/62 , C07C1/24 , B01J2229/186 , B01J2229/12 , C10G2300/4006 , C07C2529/40
Abstract: The present invention is in the field of processes for the production of BioLPG, and catalysts for use in said processes.
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4.
公开(公告)号:US20230405559A1
公开(公告)日:2023-12-21
申请号:US18335772
申请日:2023-06-15
Inventor: Matteo CARGNELLO , Aisulu AITBEKOVA
CPC classification number: B01J23/42 , B01J23/44 , B01J21/04 , B01J35/0013 , B01J35/006 , B01J37/0018 , B01J37/0211 , B01J37/0205 , B01J37/086 , B01J37/0213 , B01J37/0236 , B01J37/024 , B01D53/86 , B01D2255/1021 , B01D2255/1023
Abstract: One or more embodiments relate to stable catalysts prepared through the encapsulation of platinum particles inside an alumina framework. These catalysts do not sinter at 800° C. in the presence of oxygen and steam, conditions in which conventional catalysts sinter to large extents, while showing similar reaction rates. Extending this approach to Pd/Pt bimetallic catalysts leads to maintained small particle size at temperatures as high as 1,100° C. in air and steam. This strategy can be broadly applied to other metal and metal oxides for applications where sintering is a major cause of materials deactivation.
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公开(公告)号:US20230347320A1
公开(公告)日:2023-11-02
申请号:US17796478
申请日:2021-01-29
Applicant: Japan Science and Technology Agency
Inventor: Katsutoshi Nagaoka , Yuta Ogura , Katsutoshi Sato , Shin-ichiro Miyahara
IPC: B01J23/04 , B01J23/02 , B01J23/75 , B01J23/46 , B01J23/745 , B01J23/755 , B01J37/08 , B01J37/02 , C01C1/04
CPC classification number: B01J23/04 , B01J23/02 , B01J23/75 , B01J23/462 , B01J23/745 , B01J23/755 , B01J37/088 , B01J37/024 , B01J37/0205 , C01C1/0411
Abstract: A composite oxide including an oxide of a metal element L and an oxide of a metal element N, and represented by a composition of general formula LnN1-n, wherein the metal element L is a Group 1 element, a Group 2 element, or a Group 1 element and a Group 2 element, the metal element N comprises a Group 1 or Group 2 element other than the metal element L, n is 0.001 or more and 0.300 or less, the oxide of the metal element L and the oxide of the metal element N form no solid solution, and oxide particles of the metal element L are deposited on surfaces of oxide particles of the metal element N. Also, a metal-carrier material and an ammonia synthesis catalyst having, supported on this composite oxide, particles of at least one metal M selected from the group consisting of cobalt, iron, and nickel.
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公开(公告)号:US11701643B2
公开(公告)日:2023-07-18
申请号:US17367764
申请日:2021-07-06
Applicant: CLARIANT INTERNATIONAL LTD
Inventor: Rong Xing , Vladimir Fridman
CPC classification number: B01J23/896 , B01J21/12 , B01J23/63 , B01J23/6562 , B01J37/024 , B01J37/0205 , B01J37/088 , C07C5/3337 , C07C2521/04 , C07C2523/63 , C07C2523/656 , C07C2523/89
Abstract: The present disclosure relates to gallium-based dehydrogenation catalysts that further include additional metal components, and to methods for dehydrogenating hydrocarbons using such catalysts. One aspect of the disclosure provides a calcined dehydrogenation catalyst that includes a gallium species, a cerium species, a platinum promoter, and a silica-alumina support. Optionally, the composition can include a promoter selected from the alkali metals and alkaline earth metals.
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7.
公开(公告)号:US20180326400A1
公开(公告)日:2018-11-15
申请号:US15776837
申请日:2016-11-11
Applicant: Evonik Roehm GmbH
Inventor: Alexander LYGIN , Steffen KRILL , Matthias GROEMPING , Andreas TEPPERIS
IPC: B01J21/04 , B01J21/08 , B01J23/89 , B01J23/52 , B01J35/00 , B01J35/02 , B01J35/10 , B01J37/02 , B01J37/06 , B01J37/08 , B01J37/14
CPC classification number: B01J21/04 , B01J21/08 , B01J21/10 , B01J23/52 , B01J23/8906 , B01J23/8913 , B01J35/006 , B01J35/0066 , B01J35/008 , B01J35/023 , B01J35/1019 , B01J35/1057 , B01J35/1061 , B01J37/0201 , B01J37/0205 , B01J37/0207 , B01J37/0211 , B01J37/024 , B01J37/06 , B01J37/08 , B01J37/12 , B01J37/14 , B01J2231/49 , B01J2523/19 , B01J2523/27 , B01J2523/842 , B01J2523/845 , C07C67/39 , C07C67/42 , C07C69/54
Abstract: The present invention relates to novel catalysts for oxidative esterification, by means of which, for example, (meth)acrolein can be converted to methyl (meth)acrylate. The catalysts of the invention are especially notable for high mechanical and chemical stability even over very long periods. This especially relates to an improvement in the catalyst service life, activity and selectivity over prior art catalysts which lose activity and/or selectivity relatively quickly in continuous operation in media having even a small water content.
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公开(公告)号:US20180318811A1
公开(公告)日:2018-11-08
申请号:US15963303
申请日:2018-04-26
Applicant: ExxonMobil Research and Engineering Company
Inventor: Chuansheng BAI , Paul PODSIADLO , Stephen J. McCARTHY
CPC classification number: B01J29/48 , B01J29/076 , B01J29/7861 , B01J35/1019 , B01J37/0203 , B01J37/0236 , B01J37/024 , B01J37/18 , B01J37/20 , B01J2229/186 , B01J2229/20 , B01J2229/34 , B01J2229/42 , C10G45/64 , C10G65/043
Abstract: Methods, catalysts, and corresponding catalyst precursors are provided for performing dewaxing of diesel or distillate boiling range fractions. The dewaxing methods, catalysts, and/or catalyst precursors can allow for production of diesel boiling range fuels with improved cold flow properties at desirable yields. The catalysts and/or catalyst precursors can correspond to supported metal catalysts and/or catalyst precursors that include at least one noble metal, such as Pt, at least one Group 8-10 base metal, preferably a non-noble Group 8-10 base metal, such as Ni and/or Co along with a Group 6 metal, such as Mo and/or W as supported metals along. The support can include a zeolitic framework structure. The catalyst precursors can be formed, for example, by impregnating a support including a zeolitic framework structure with impregnation solution(s) that also includes a dispersion agent.
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公开(公告)号:US20180290131A1
公开(公告)日:2018-10-11
申请号:US15570661
申请日:2016-03-11
Applicant: IFP Energies nouvelles
Inventor: Pierre-Louis CARRETTE
CPC classification number: B01J31/0209 , B01J21/04 , B01J23/85 , B01J23/882 , B01J27/19 , B01J31/04 , B01J35/1019 , B01J35/1042 , B01J35/1061 , B01J37/0009 , B01J37/0201 , B01J37/0203 , B01J37/0205 , B01J37/0236 , B01J37/024 , B01J37/08 , B01J37/20 , B01J37/28 , B01J2523/00 , C10G45/08 , C10G47/20 , B01J2523/31 , B01J2523/51 , B01J2523/68 , B01J2523/845
Abstract: The invention relates to a catalyst comprising a support based on alumina or silica or silica-alumina, at least one element of group VIII, at least one element of group VIB and at least one additive selected from γ-valerolactone, 4-hydroxyvaleric acid, 2-pentenoic acid, 3-pentenoic acid or 4-pentenoic acid. The invention also relates to the process for the preparation of said catalyst and the use thereof in a hydrotreatment and/or hydrocracking process.
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10.
公开(公告)号:US10058852B2
公开(公告)日:2018-08-28
申请号:US14790678
申请日:2015-07-02
Applicant: IFP Energies nouvelles
Inventor: Antoine Daudin
IPC: B01J27/19 , B01J37/02 , B01J35/10 , C10G45/08 , B01J21/04 , B01J23/882 , C10G69/04 , B01J23/883
CPC classification number: B01J27/19 , B01J21/04 , B01J23/882 , B01J23/883 , B01J35/1014 , B01J35/1019 , B01J37/0201 , B01J37/0205 , B01J37/0236 , B01J37/024 , C10G45/08 , C10G69/04
Abstract: The present invention concerns a hydrotreatment catalyst comprising an alumina-based support, at least one metal from group VIB, at least one metal from group VIII and phosphorus, in which: the specific surface area of the catalyst is in the range 20 to 150 m2/g; the density of the metal from group VIB, expressed as the number of atoms of metal from group VIB per unit surface area of catalyst, is in the range 7 to 30 atoms of metal from group VIB per nm2 of catalyst; the catalyst being prepared by impregnation of the metals from group VIB, group VIII and phosphorus onto the support in order to obtain an impregnated catalyst precursor, then drying said impregnated catalyst precursor at a temperature of less than 200° C. and without subsequent calcining.
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