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31.
公开(公告)号:US20180148657A1
公开(公告)日:2018-05-31
申请号:US15878626
申请日:2018-01-24
Applicant: INSTITUTO MEXICANO DEL PETROLEO
Inventor: Patricia RAYO MAYORAL , Jorge ANCHEYTA JUAREZ , Gustavo Jesus MARROQUIN SANCHEZ , Guillermo CENTENO NOLASCO , Jorge Fernando RAMIREZ SOLIS
IPC: C10G47/20 , C10G45/12 , B01J21/12 , C10G45/08 , B01J23/883 , B01J29/03 , B01J29/035 , B01J37/08 , B01J37/02 , B01J35/10 , B01J35/02 , B01J29/80 , B01J29/16 , B01J29/14 , B01J29/10 , B01J29/08 , B01J29/04 , B01J37/00
CPC classification number: C10G47/20 , B01J21/12 , B01J23/883 , B01J29/0308 , B01J29/0356 , B01J29/0358 , B01J29/041 , B01J29/044 , B01J29/045 , B01J29/084 , B01J29/106 , B01J29/146 , B01J29/166 , B01J29/80 , B01J35/026 , B01J35/1019 , B01J35/1038 , B01J35/1042 , B01J35/1057 , B01J35/1061 , B01J35/109 , B01J37/0018 , B01J37/0201 , B01J37/08 , B01J2229/186 , C10G45/08 , C10G45/10 , C10G45/12 , C10G47/14 , C10G47/16 , C10G47/18
Abstract: A hydrocracking catalyst having a support of a composite of mesoporous materials, molecular sieves and alumina, is used in the last bed of a multi-bed system for treating heavy crude oils and residues and is designed to increase the production of intermediate distillates having boiling points in a temperature range of 204° C. to 538° C., decrease the production of the heavy fraction (>538° C.), and increase the production of gasoline fraction (
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公开(公告)号:US09976098B2
公开(公告)日:2018-05-22
申请号:US14782957
申请日:2014-04-08
Applicant: SK Innovation Co., Ltd. , SK Lubricants Co., Ltd.
Inventor: Hee Jung Jeon , Ja Hyun Yang , Tae Jin Kim , Young Hwan Lee , Jong Chan Lee , Wan Seop Kwon , Jin Hee Ok
IPC: C10M135/34 , C10M105/34 , C10G45/00 , C07C1/00 , C07C4/00 , C10G1/00 , C10M105/24 , C10M107/08 , C10M177/00 , C10M107/10 , C10G69/12 , C10G3/00 , B01J23/44 , B01J29/08 , B01J35/00 , B01J35/10
CPC classification number: C10M105/24 , B01J23/44 , B01J29/084 , B01J35/0026 , B01J35/1019 , B01J35/1042 , B01J35/1061 , B01J2229/34 , C10G3/44 , C10G69/126 , C10G2300/1011 , C10G2400/10 , C10M107/08 , C10M107/10 , C10M177/00 , C10M2205/0285 , C10N2220/022 , C10N2230/02 , Y02P30/20
Abstract: Disclosed is a method for producing a quality lubricant base oil (meeting the standard of Group III or higher) comprising: decarbonylating mixed fatty acids derived from oils and fats of biological origin to produce mixed olefins; oligomerizing the mixed olefins to produce an olefinic lubricant base oil; and performing hydrogenation to remove olefins from the olefinic lubricant base oil.
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公开(公告)号:US09956543B2
公开(公告)日:2018-05-01
申请号:US14913077
申请日:2014-04-25
Applicant: DAIICHI KIGENSO KAGAKU KOGYO CO., LTD.
Inventor: Hiroshi Kodama
CPC classification number: B01J21/066 , B01J23/10 , B01J35/1014 , B01J35/1038 , B01J35/1042 , B01J35/1061 , B01J35/1066 , B01J37/031 , B01J37/04 , B01J37/08 , B01J37/20 , C01G25/02 , C01P2004/03 , C01P2004/32 , C01P2006/12 , C01P2006/13 , C01P2006/14 , C01P2006/16 , C01P2006/17
Abstract: This invention provides a zirconia-based porous body having a pore diameter suitable for supporting catalytic active species, such as precious metals, small variability in pore diameter, and a sufficient specific surface area even after 12-hour heating at 1000° C. Specifically, the invention provides a zirconia-based porous body in particle form having (1) a pore diameter peak at 20 to 100 nm in the pore distribution by BJH method, a P/W ratio of 0.05 or more wherein W represents half width of the peak and P represents height of the peak in the measured pore distribution curve, and a total pore volume of 0.5 cm3/g or more; and (2) a pore diameter peak at 20 to 100 nm, the P/W ratio of 0.03 or more, a specific surface area of at least 40 m2/g, and a total pore volume of 0.3 cm3/g or more, after heat treatment at 1000° C. for 12 hours.
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公开(公告)号:US09950968B2
公开(公告)日:2018-04-24
申请号:US15128243
申请日:2015-04-01
Applicant: Technip E&C Limited
Inventor: Stephen Roy Partington , Nigel Stewart Brown , Michael Keith Lee , Mark Julian Howard
IPC: C07C1/24 , B01J23/30 , B01J35/10 , B01J37/02 , B01J27/188
CPC classification number: C07C1/24 , B01J23/30 , B01J27/188 , B01J35/1019 , B01J35/1042 , B01J35/1061 , B01J37/0201 , B01J2523/00 , C07C2523/30 , Y02P20/52 , C07C11/04 , B01J2523/41 , B01J2523/69
Abstract: The present invention provides a process for the preparation of ethene by vapor phase chemical dehydration of a feed comprising ethanol, said process comprising contacting the feed with a supported heteropolyacid catalyst in a reactor, wherein the feed temperature is at least 250° C. and the pressure inside the reactor is at least 0.80 MPa but less than 1.80 MPa.
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公开(公告)号:US20180104672A1
公开(公告)日:2018-04-19
申请号:US15565913
申请日:2016-02-22
Applicant: IFP Energies Nouvelles
Inventor: Romain CHENEVIER , Dominique DECOTTIGNIES , Vincent LECOCQ , Marie VELLY
CPC classification number: B01J23/75 , B01J21/005 , B01J21/02 , B01J21/12 , B01J23/005 , B01J23/462 , B01J23/745 , B01J23/755 , B01J35/0006 , B01J35/1014 , B01J35/1019 , B01J35/1038 , B01J35/1042 , B01J37/0201 , B01J37/0207 , B01J37/0236 , B01J37/024 , B01J37/08 , B01J37/14 , C10G2/332
Abstract: A catalyst containing an active phase comprising at least one metal of group VIIIB selected from cobalt, nickel, ruthenium and iron deposited on a support containing silica, alumina and at least one simple spinel MAl2O4 or mixed spinel MxM′(1−x)Al2O4) which is or is not partial, wherein M and M′ are separate metals selected from the group formed by magnesium, copper, cobalt, nickel, tin, zinc, lithium, calcium, caesium, sodium, potassium, iron and manganese, and wherein x is between 0 and 1, the values 0 and 1 being themselves excluded, characterised in that said active phase further comprises boron, the boron content being between 0.001% and 0.5% by weight with respect to the total weight of the catalyst, the value 0.5 being itself excluded.
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公开(公告)号:US09937485B2
公开(公告)日:2018-04-10
申请号:US15335586
申请日:2016-10-27
Applicant: CHINA PETROLEUM & CHEMICAL CORPORATION , FUSHUN RESEARCH INSTITUTE OF PETROLEUM AND PETROCHEMICALS, SINOPEC
Inventor: Yanze Du , Minghua Guan , Fenglai Wang , Chang Liu
IPC: B01J37/06 , C10G47/12 , B01J23/883 , B01J21/12 , B01J23/28 , B01J23/30 , B01J23/75 , B01J23/755 , B01J23/85 , B01J23/888 , B01J29/072 , B01J29/076 , B01J35/00 , B01J35/10 , B01J37/00 , B01J37/02 , B01J37/03 , B01J37/04 , C10G47/20 , C10G65/12 , B01J37/08 , B01J29/04 , B01J29/14 , B01J29/16 , B01J29/46 , B01J29/48 , B01J29/76 , B01J29/78 , B01J29/85
CPC classification number: B01J23/883 , B01J21/12 , B01J23/28 , B01J23/30 , B01J23/75 , B01J23/755 , B01J23/85 , B01J23/888 , B01J23/8885 , B01J29/044 , B01J29/045 , B01J29/072 , B01J29/076 , B01J29/146 , B01J29/166 , B01J29/46 , B01J29/48 , B01J29/7615 , B01J29/7815 , B01J29/85 , B01J35/002 , B01J35/0093 , B01J35/1019 , B01J35/1023 , B01J35/1038 , B01J35/1042 , B01J35/1047 , B01J35/1061 , B01J37/0009 , B01J37/0018 , B01J37/009 , B01J37/0201 , B01J37/0213 , B01J37/0236 , B01J37/036 , B01J37/04 , B01J37/08 , B01J2229/16 , B01J2229/36 , B01J2229/37 , C10G47/12 , C10G47/20 , C10G65/12 , C10G2300/1074 , C10G2300/301 , C10G2300/4018
Abstract: The present invention relates to a hydrocracking catalyst, a process for preparing the same and use thereof. The present catalyst comprises a cracking component and a hydrogenation component, wherein the cracking component comprises from 0 to 20 wt. % of a molecular sieve and from 20 wt. % to 60 wt. % of an amorphous silica-alumina, the hydrogenation component comprises at least one hydrogenation metal in a total amount of from 34 wt. % to 75 wt. % calculated by the mass of oxides, each amount is based on the total weight of the catalyst. The present catalyst is prepared by directly mixing an acidic component powder material with an impregnating solution, impregnating, filtering, drying, molding, and drying and calcining.
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公开(公告)号:US20180093933A1
公开(公告)日:2018-04-05
申请号:US15832064
申请日:2017-12-05
Applicant: Borealis AG
Inventor: Mariana Stoyanova , Evgeny Kondratenko , David Linke , Eberhard Ernst
IPC: C07C6/04 , B01J21/08 , B01J35/10 , B01J23/28 , B01J23/30 , B01J35/00 , B01J37/16 , B01J35/02 , B01J37/14 , C07C11/08 , B01J37/08 , C07C11/04 , B01J37/18 , B01J23/02 , B01J37/00 , B01J37/04 , B01J37/12
CPC classification number: C07C6/04 , B01J21/08 , B01J21/10 , B01J23/02 , B01J23/28 , B01J23/30 , B01J35/0006 , B01J35/002 , B01J35/023 , B01J35/1014 , B01J35/1019 , B01J35/1038 , B01J35/1042 , B01J35/1061 , B01J37/0027 , B01J37/04 , B01J37/08 , B01J37/12 , B01J37/14 , B01J37/16 , B01J37/18 , B01J2231/52 , B01J2231/543 , C07C2521/08 , C07C2521/10 , C07C2523/02 , C07C2523/04 , C07C2523/30 , Y02P20/52 , C07C11/08 , C07C11/04
Abstract: The present invention relates to a magnesium oxide (MgO) catalyst for isomerisation of olefins with defined physical properties. The present invention further relates to a catalyst for conversion of olefins having a first catalyst component and a second catalyst component. The first catalyst component has a metathesis catalyst. The second catalyst component has the magnesium oxide catalyst. A process for obtaining an olefin is also disclosed.
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公开(公告)号:US20180065108A1
公开(公告)日:2018-03-08
申请号:US15561220
申请日:2016-03-25
Applicant: BASF Corporation
Inventor: Deepak S. THAKUR , William O. Tuttle , Arunabha Kundu , Keenan Lee Deutsch , Jeffrey Baciak
CPC classification number: B01J23/002 , B01J21/14 , B01J23/70 , B01J23/72 , B01J23/80 , B01J23/8892 , B01J35/002 , B01J35/0026 , B01J35/0066 , B01J35/1014 , B01J35/1038 , B01J35/1042 , B01J37/0018 , B01J37/04 , B01J37/08 , B01J2231/60 , B01J2523/00 , B01J2523/23 , B01J2523/27 , B01J2523/72 , B01J2523/845 , B01J2523/847 , C07C29/149 , B01J2523/17 , B01J2523/31 , B01J2523/41 , C07C33/02
Abstract: A catalyst includes a mixed metal oxide; an alumina; silica, and calcium, where the mixed metal oxide includes Cu and at least one of Mn, Zn, Ni, or Co. Such catalysts exhibit enhanced tolerance sulfur-containing compounds and free fatty acids.
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公开(公告)号:US09908102B2
公开(公告)日:2018-03-06
申请号:US14683070
申请日:2015-04-09
Applicant: Indian Institute of Technology Kanpur
Inventor: Ashutosh Sharma , Shishir Katiyar , Kunal Mondal
IPC: B01J21/08 , B01J21/18 , B01J23/50 , B01J31/06 , B01J35/00 , B01J35/04 , B01J35/10 , B01J37/00 , B01J37/02 , B01J37/03 , B01J37/04 , B01J37/08 , B01J23/38 , B01J23/70
CPC classification number: B01J23/50 , B01J21/08 , B01J21/18 , B01J23/38 , B01J23/70 , B01J31/06 , B01J35/0013 , B01J35/002 , B01J35/006 , B01J35/04 , B01J35/1023 , B01J35/1028 , B01J35/1038 , B01J35/1042 , B01J35/1047 , B01J35/1061 , B01J37/0018 , B01J37/036 , B01J37/04 , B01J37/084 , B01J2229/32 , B01J2231/64 , B01J2531/002 , B01J2531/005
Abstract: Methods of forming a hierarchical porous monolith are provided. The methods include mixing a monomer, a silica precursor and a catalyst in a solvent to form a mixture. The methods also include adding a gelling agent to the mixture to form a polymer-silica composite gel. The polymer-silica composite gel undergoes a phase separation to separate from the solvent and the unreacted silica precursor. The method further includes drying the polymer-silica composite gel to evaporate the solvent to form a polymer-silica monolith and processing the polymer-silica monolith to form at least one of a polymer monolith, a carbon monolith, a silica monolith and a carbon-silica monolith.
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公开(公告)号:US20180050325A1
公开(公告)日:2018-02-22
申请号:US15557578
申请日:2016-03-30
Applicant: BASF Corporation
Inventor: Keenan Lee Deutsch , Rostam J. MADON
IPC: B01J23/843 , B01J21/08 , B01J35/00 , B01J35/10 , B01J37/02 , B01J37/08 , B01J37/16 , C07C29/141
CPC classification number: B01J23/8437 , B01J21/08 , B01J23/72 , B01J35/0006 , B01J35/0066 , B01J35/026 , B01J35/08 , B01J35/1038 , B01J35/1042 , B01J35/1047 , B01J37/0018 , B01J37/0201 , B01J37/0203 , B01J37/0236 , B01J37/086 , B01J37/088 , B01J37/16 , C07C29/141 , C07C29/154 , C07C29/44 , C07C33/046 , C07C31/12
Abstract: A process for preparing a catalyst includes impregnating a metal oxide carrier with an aqueous solution to form an impregnated carrier; drying the impregnated carrier to form a dried, impregnated carrier; and heat-treating the dried, impregnated carrier in air to form the catalyst; wherein: the aqueous solution includes a copper salt; and from about 3 wt % to about 15 wt % of a C3-C6 multifunctional carboxylic acid; and the catalyst includes from about 5 wt % to about 50 wt % copper oxide.
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