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公开(公告)号:US11999814B2
公开(公告)日:2024-06-04
申请号:US18065003
申请日:2022-12-13
Applicant: Chevron Phillips Chemical Company LP
Inventor: Max P. McDaniel , Qing Yang , Ryan N. Rose , Kathy S. Clear , Graham R. Lief , Eric D. Schwerdtfeger , Anand Ramanathan , Jeremy M. Praetorius , Connor D. Boxell
IPC: C08F4/02 , C08F4/659 , C08F4/6592 , C08F210/02
CPC classification number: C08F4/025 , C08F4/65916 , C08F4/65925 , C08F4/65927 , C08F210/02 , C08F2420/01 , C08F2420/03
Abstract: Sulfated bentonite compositions are characterized by a total pore volume from 0.4 to 1 mL/g, a total BET surface area from 200 to 400 m2/g, and an average pore diameter from 55 to 100 Angstroms. The sulfated bentonite compositions also can be characterized by a d50 average particle size in a range from 15 to 50 μm and a ratio of d90/d10 from 3 to 15. The sulfated bentonite compositions can contain a sulfated bentonite and from 10 to 90 wt. % of colloidal particles, or the sulfated bentonite compositions can contain a sulfated bentonite and from 0.2 to 10 mmol/g of zinc and/or phosphorus. These compositions can be utilized in metallocene catalyst systems to produce ethylene based polymers.
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2.
公开(公告)号:US11999807B2
公开(公告)日:2024-06-04
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
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.
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公开(公告)号:US11969718B2
公开(公告)日:2024-04-30
申请号:US18167129
申请日:2023-02-10
Applicant: Chevron Phillips Chemical Company LP
Inventor: Masud M. Monwar , Carlos A. Cruz , Jared L. Barr , Max P. McDaniel
IPC: C08F110/02 , B01J8/08 , B01J8/18 , B01J19/12 , B01J31/12 , C08F4/78 , C08F10/02 , C08F210/16 , B01J21/08 , B01J23/26 , B01J31/34 , B01J37/16 , B01J37/34 , C08F4/22
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 , B01J2219/0869 , B01J2219/089 , B01J2219/1203 , B01J2531/62 , C08F4/22 , 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.
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公开(公告)号:US11865505B2
公开(公告)日:2024-01-09
申请号:US17588398
申请日:2022-01-31
Applicant: Chevron Phillips Chemical Company LP
Inventor: Max P. McDaniel , Kathy S. Clear , Jeremy M. Praetorius
IPC: B01J23/26 , B01J35/10 , C08F10/02 , B01J37/02 , B01J35/02 , B01J37/03 , B01J37/14 , B01J21/06 , B01J21/08 , C08F4/18 , C08F4/24 , C08F10/00 , B01J3/02 , B01J31/34 , B01J31/38 , B01J37/04 , B01J31/02
CPC classification number: B01J23/26 , B01J21/063 , B01J21/08 , B01J35/023 , B01J35/1019 , B01J35/1023 , B01J35/1042 , B01J35/1047 , B01J37/0203 , B01J37/0207 , B01J37/0209 , B01J37/035 , B01J37/04 , C08F4/18 , C08F4/24 , C08F10/00 , C08F10/02 , B01J31/0212 , B01J31/0274 , B01J31/0275 , B01J31/34 , B01J31/38 , B01J2231/12 , C08F10/00 , C08F4/24 , C08F110/02 , C08F2500/12
Abstract: Methods for synthesizing a water-soluble titanium-silicon complex are disclosed herein. The titanium-silicon complex can be utilized to produce titanated solid oxide supports and titanated chromium supported catalysts. The titanated chromium supported catalysts subsequently can be used to polymerize olefins to produce, for example, ethylene based homopolymer and copolymers.
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5.
公开(公告)号:US11814457B2
公开(公告)日:2023-11-14
申请号:US18167120
申请日:2023-02-10
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
IPC: B01J31/38 , B01J31/00 , C08F4/64 , C08F210/16 , C08J5/18 , C08F4/6592 , B01J3/00 , B01J37/26 , B01J35/02
CPC classification number: C08F210/16 , B01J31/38 , C08J5/18 , B01J3/00 , B01J35/023 , B01J37/26 , C08F4/6592 , C08F4/65925 , C08F4/65927 , C08F2410/07 , C08F2500/12 , C08F2500/26 , C08J2323/20
Abstract: Catalyst compositions containing a metallocene compound, a solid activator, and a co-catalyst, in which the solid activator or the supported metallocene catalyst has a d50 average particle size of 15 to 50 μm and a particle size distribution of 0.5 to 1.5, can be contacted with an olefin in a loop slurry reactor to produce an olefin polymer. A representative ethylene-based polymer produced using the catalyst composition has excellent dart impact strength and low gels, and can be characterized by a HLMI from 4 to 10 g/10 min, a density from 0.944 to 0.955 g/cm3, a higher molecular weight component with a Mn from 280,000 to 440,000 g/mol, and a lower molecular weight component with a Mw from 30,000 to 45,000 g/mol and a ratio of Mz/Mw ranging from 2.3 to 3.4.
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6.
公开(公告)号:US20230356206A1
公开(公告)日:2023-11-09
申请号:US18358088
申请日:2023-07-25
Inventor: Carlos A. Cruz , Mitchell D. Refvik , Max P. McDaniel , Mark Scott , Evan Merk
CPC classification number: B01J37/0045 , B01J35/023 , B01J35/1004
Abstract: Methods for modifying a catalyst system component are disclosed in which a feed mixture containing a fluid and from 1 to 15 wt. % of a catalyst system component is introduced into an inlet of a hydrocyclone, an overflow stream containing from 0.1 to 5 wt. % solids and an underflow stream containing from 10 to 40 wt. % solids are discharged from the hydrocyclone, and the underflow stream is spray dried to form a modified catalyst component. Often, from 4 to 20 wt. % of the catalyst system component in the feed mixture has a particle size of less than or equal to 20 μm, or less than or equal to 10 μm.
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公开(公告)号:US20230192914A1
公开(公告)日:2023-06-22
申请号:US17552451
申请日:2021-12-16
Applicant: Chevron Phillips Chemical Company LP
Inventor: Max P. McDaniel , Graham R. Lief , Qing Yang , Carlos A. Cruz , Yongwoo Inn , Jared Barr
Abstract: Methods for controlling the long chain branch content of ethylene homopolymers and copolymers produced in a polymerization process include the steps of contacting a metallocene compound, an organoaluminum compound, a high LCB activator-support, and a low LCB activator-support to form a catalyst composition, contacting the catalyst composition with ethylene and an optional olefin comonomer in a polymerization reactor system under polymerization conditions to produce an ethylene polymer having a LCB content, and controlling the relative amount of the high LCB activator-support and the low LCB activator-support in the catalyst composition to adjust the LCB content of the ethylene polymer.
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8.
公开(公告)号:US11548958B2
公开(公告)日:2023-01-10
申请号:US17748116
申请日:2022-05-19
Applicant: Chevron Phillips Chemical Company LP
Inventor: Max P. McDaniel , Kathy S. Clear , Carlton E. Ash , Stephen L. Kelly , Amanda B. Allemand
IPC: C08F10/02
Abstract: Silica composites and supported chromium catalysts having a bulk density of 0.08 to 0.4 g/mL, a total pore volume of 0.4 to 2.5 mL/g, a BET surface area of 175 to 375 m2/g, and a peak pore diameter of 10 to 80 nm are disclosed herein. These silica composites and supported chromium catalysts can be formed by combining two silica components. The first silica component can be irregularly shaped, such as fumed silica, and the second silica component can be a colloidal silica or a silicon-containing compound, and the second silica component can act as a glue to bind the silica composite together.
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9.
公开(公告)号:US11512154B2
公开(公告)日:2022-11-29
申请号:US17716027
申请日:2022-04-08
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
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.
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公开(公告)号:US20220348527A1
公开(公告)日:2022-11-03
申请号:US17867782
申请日:2022-07-19
Applicant: Chevron Phillips Chemical Company LP
Inventor: Carlos A. Cruz , Masud M. Monwar , Max P. McDaniel , Jared Barr , Kathy S. Clear , William C. Ellis
IPC: C07C29/72 , B01J23/26 , B01J21/06 , B01J21/08 , B01J38/02 , C07C29/50 , C07C37/58 , C07C45/33 , C07C51/215 , C07C31/20 , B01J37/08 , C07C29/48 , C07C29/09 , B01J37/34
Abstract: Processes for converting a hydrocarbon reactant into an alcohol compound and/or a carbonyl compound are disclosed, and these processes include the steps of forming a supported chromium catalyst comprising chromium in a hexavalent oxidation state, irradiating the hydrocarbon reactant and the supported chromium catalyst with a light beam at a wavelength in the UV-visible spectrum to reduce at least a portion of the supported chromium catalyst to form a reduced chromium catalyst, and hydrolyzing the reduced chromium catalyst to form a reaction product comprising the alcohol compound and/or the carbonyl compound. The supported chromium catalyst can be formed by heat treating a supported chromium precursor, contacting a chromium precursor with a solid support while heat treating, or heat treating a solid support and then contacting a chromium precursor with the solid support.
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