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公开(公告)号：US12203036B2
公开(公告)日：2025-01-21
申请号：US17917533
申请日：2021-04-06
Applicant: TotalEnergies OneTech Belgium
Inventor： Cindy Adam , Delphine Minoux , Walter Vermeiren , Sébastien Leplat , Emmanuel Van Loock , Christophe Breton
IPC: C10G65/12 , B01J20/08 , B01J23/755 , B01J23/883 , B01J35/61 , C07C4/04 , C10G1/00 , C10G1/10 , C10G11/18 , C10G31/08 , C10G33/00 , C10G45/08 , C10G45/10 , C10G45/40 , C10G45/44 , C10G65/06 , C10G67/06 , C10G67/14 , C10G69/06 , C10G69/10
Abstract: A process to produce olefins and aromatics via a purification of a hydrocarbon stream including: a) Providing a hydrocarbon stream having a starting boiling point of at least 15° C., a diene value of at least 1.0 preferably at least 1.5 g I2/100 g and a bromine number of at least 5 g Br2/100 g and containing at least 10 wt % of pyrolysis plastic oil where preferably at least 10 wt. % of said hydrocarbon stream has a boiling point of at least 150° C. based on the total weight of said hydrocarbon stream; c) Performing a first hydrotreating step; e) performing a second hydrotreating step; and f) recovering a purified hydrocarbon stream wherein at least a part of this purified hydrocarbon stream is sent to a steam cracker to produce olefins, such as ethylene and propylene, and aromatics.
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公开(公告)号：US12122965B2
公开(公告)日：2024-10-22
申请号：US18000578
申请日：2021-07-06
Applicant: TOPSOE A/S
Inventor： Christian Frederik Weise , Michal Lutecki , Frank Bartnik Johansson
CPC classification number: C10G67/06 , B01J20/08 , B01J20/28042 , B01J20/28059 , B01J20/28061 , B01J20/28073 , B01J20/28088 , C10G2300/1011 , C10G2300/1033 , C10G2300/202
Abstract: A porous material including alumina, the alumina including alpha-alumina, the porous material including one or more metals selected from Co, Mo, Ni, W and combinations thereof, and the porous material having a BET-surface area of 1-110 m2/g, a total pore volume of 0.50-0.80 ml/g, as measured by mercury intrusion porosimetry, and a pore size distribution (PSD) with at least 30 vol % of the total pore volume being in pores with a radius ≥400 Å, suitably pores with a radius ≥500 Å. A process for removing impurities such as phosphorous (P) from a feedstock, by contacting the feedstock with a guard bed including the above porous material. A guard bed for a hydrotreatment system including the porous material, a hydrotreatment system including a guard bed which includes the porous material and a downstream hydrotreatment section including at least one hydrotreatment catalyst.
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公开(公告)号：US12077714B2
公开(公告)日：2024-09-03
申请号：US16710856
申请日：2019-12-11
Applicant: SAUDI ARABIAN OIL COMPANY
Inventor： Omer Refa Koseoglu , Ali Alzaid
CPC classification number: C10B57/06 , C10B57/045 , C10B57/005
Abstract: A process for the treatment of a hydrocracking unit bottoms stream containing heavy poly-nuclear aromatic (HPNA) compounds and/or a fresh hydrocracking feedstock stream containing HPNA precursors to produce coke. The HPNA and/or HPNA precursors are removed from the hydrocracking unit bottoms stream and/or a fresh hydrocracking feedstock stream by solvent washing, and the HPNA and/or HPNA precursors are subjected to delayed coking for the production of coke.
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4.发明公开公开(公告)号：US20240199963A1
公开(公告)日：2024-06-20
申请号：US18288944
申请日：2022-05-02
Applicant: TotalEnergies OneTech
Inventor： Thomas COUSTHAM , Christine LEGRAND , Hélène COULOMBEAU-LEROY
CPC classification number: C10G67/06 , B01J8/02 , B01J20/02 , B01J20/28011 , B01J20/34 , C10G2300/1014 , C10G2300/202 , C10G2300/4006 , C10G2300/4012 , C10G2300/70
Abstract: Disclosed is a method for purifying a composition containing a plastic pyrolysis oil, which method comprises treating with a strong base in the presence of an alcohol. The method is useful for reducing the concentration of heteroelements in said composition with a view to making it compatible for introduction as feedstock in conversion methods such as steam cracking, fluid catalytic cracking, catalytic hydrogenation or hydrocracking.
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公开(公告)号：US20240043757A1
公开(公告)日：2024-02-08
申请号：US18462645
申请日：2023-09-07
Applicant: Magëmä Technology LLC
Inventor： Michael Joseph Moore , Bertrand Ray Klussmann , Carter James White
IPC: C10G45/04 , C10G67/06 , C10G45/22 , C10G45/08 , C10G25/02 , C10G25/00 , B01D3/34 , B01J8/04 , C10G65/04 , C10L1/12 , C10L1/14 , C10L1/16 , B01D53/14 , C10G7/00 , C10G45/06 , C10L1/04 , C10G45/02 , C10G67/02 , B01J8/00 , B01J21/04 , B01J23/24 , B01J23/40 , B01J23/74 , C10G65/16 , B01J8/02 , C10G47/02 , C10G69/02
CPC classification number: C10G45/04 , C10G67/06 , C10G45/22 , C10G45/08 , C10G25/02 , C10G25/003 , B01D3/343 , B01J8/0492 , C10G65/04 , C10L1/12 , C10L1/14 , C10L1/1608 , B01D53/1481 , C10G7/00 , C10G45/06 , C10L1/04 , C10G45/02 , C10G67/02 , B01J8/008 , B01J8/0457 , B01J21/04 , B01J23/24 , B01J23/40 , B01J23/74 , C10G65/16 , B01J8/0278 , B01J8/0292 , C10G47/02 , C10G69/02 , C10G2300/302 , C10G2300/202 , C10G2300/1059 , B01J2208/025 , C10G2300/207 , C10G2300/30 , C10G2300/4012 , C10G2300/4018 , C10G2300/70 , C10G2300/80 , C10L2270/026 , C10G2300/107 , C10G2300/1077 , C10G2300/1048 , C10G2400/06 , C10L2200/0263 , C10L2270/02 , C10G2300/205 , C10L2200/0438 , B01J2208/00557 , C10G2300/1044 , C10G2300/308 , C10G2300/4062 , C10G2400/04 , C10G2300/208 , B01J2208/02 , C10G2300/1037 , C10G2300/201 , C10G2300/206
Abstract: A multi-stage process for the production of an ISO 8217 compliant Product Heavy Marine Fuel Oil from ISO 8217 compliant Feedstock Heavy Marine Fuel Oil involving a Reaction System composed of one or more reactor vessels selected from a group reactor wherein said one or more reactor vessels contains one or more reaction sections configured to promote the transformation of the Feedstock Heavy Marine Fuel Oil to the Product Heavy Marine Fuel Oil. The Product Heavy Marine Fuel Oil has a Environmental Contaminate level has a maximum sulfur content (ISO 14596 or ISO 8754) between the range of 0.05 mass % to 1.0 mass. A process plant for conducting the process for conducting the process is disclosed that can utilize a modular reactor vessel.
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Patent Agency Ranking
公开(公告)号：US11884883B2
公开(公告)日：2024-01-30
申请号：US17942906
申请日：2022-09-12
Applicant: Magêmã Technology LLC
Inventor： Michael Joseph Moore , Bertrand Ray Klussmann , Carter James White
IPC: C10G45/04 , C10G67/06 , C10G45/22 , C10G45/08 , C10G25/02 , C10G25/00 , B01D3/34 , B01J8/04 , C10G65/04 , C10L1/12 , C10L1/14 , C10L1/16 , B01D53/14 , C10G7/00 , C10G45/06 , C10L1/04 , C10G45/02 , C10G67/02 , B01J8/00 , B01J21/04 , B01J23/24 , B01J23/40 , B01J23/74 , C10G65/16 , B01J8/02 , C10G47/02 , C10G69/02
CPC classification number: C10G45/04 , B01D3/343 , B01D53/1481 , B01J8/008 , B01J8/0278 , B01J8/0292 , B01J8/0457 , B01J8/0492 , B01J21/04 , B01J23/24 , B01J23/40 , B01J23/74 , C10G7/00 , C10G25/003 , C10G25/02 , C10G45/02 , C10G45/06 , C10G45/08 , C10G45/22 , C10G47/02 , C10G65/04 , C10G65/16 , C10G67/02 , C10G67/06 , C10G69/02 , C10L1/04 , C10L1/12 , C10L1/14 , C10L1/1608 , B01J2208/00557 , B01J2208/02 , B01J2208/025 , C10G2300/107 , C10G2300/1037 , C10G2300/1044 , C10G2300/1048 , C10G2300/1059 , C10G2300/1077 , C10G2300/201 , C10G2300/202 , C10G2300/205 , C10G2300/206 , C10G2300/207 , C10G2300/208 , C10G2300/30 , C10G2300/302 , C10G2300/308 , C10G2300/4012 , C10G2300/4018 , C10G2300/4062 , C10G2300/70 , C10G2300/80 , C10G2400/04 , C10G2400/06 , C10L2200/0263 , C10L2200/0438 , C10L2270/02 , C10L2270/026 , C10L1/1608 , C10L2200/0438
Abstract: A multi-stage process for the production of an ISO 8217 compliant Product Heavy Marine Fuel Oil from ISO 8217 compliant Feedstock Heavy Marine Fuel Oil involving a Reaction System composed of one or more reactor vessels selected from a group reactor wherein said one or more reactor vessels contains one or more reaction sections configured to promote the transformation of the Feedstock Heavy Marine Fuel Oil to the Product Heavy Marine Fuel Oil. The Product Heavy Marine Fuel Oil has a Environmental Contaminate level has a maximum sulfur content (ISO 14596 or ISO 8754) between the range of 0.05 mass % to 1.0 mass. A process plant for conducting the process for conducting the process is disclosed that can utilize a modular reactor vessel.
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公开(公告)号：US11549061B2
公开(公告)日：2023-01-10
申请号：US16923152
申请日：2020-07-08
Applicant: Axens
Inventor： Dominic Debonis
Abstract: The invention relates to an improved apparatus and methods for managing and utilizing light hydrocarbons utilized and created during the hydroprocessing of biological feedstocks in the making of middle distillate fuels.
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公开(公告)号：US20230002685A1
公开(公告)日：2023-01-05
申请号：US17942906
申请日：2022-09-12
Applicant: Magêmã Technology LLC
Inventor： Michael Joseph Moore , Bertrand Ray Klussmann , Carter James White
IPC: C10G45/04 , C10G67/06 , C10G45/22 , C10G45/08 , C10G25/02 , C10G25/00 , B01D3/34 , B01J8/04 , C10G65/04 , C10L1/12 , C10L1/14 , C10L1/16 , B01D53/14 , C10G7/00 , C10G45/06 , C10L1/04 , C10G45/02 , C10G67/02 , B01J8/00 , B01J21/04 , B01J23/24 , B01J23/40 , B01J23/74 , C10G65/16 , B01J8/02 , C10G47/02 , C10G69/02
Abstract: A multi-stage process for the production of an ISO 8217 compliant Product Heavy Marine Fuel Oil from ISO 8217 compliant Feedstock Heavy Marine Fuel Oil involving a Reaction System composed of one or more reactor vessels selected from a group reactor wherein said one or more reactor vessels contains one or more reaction sections configured to promote the transformation of the Feedstock Heavy Marine Fuel Oil to the Product Heavy Marine Fuel Oil. The Product Heavy Marine Fuel Oil has a Environmental Contaminate level has a maximum sulfur content (ISO 14596 or ISO 8754) between the range of 0.05 mass % to 1.0 mass. A process plant for conducting the process for conducting the process is disclosed that can utilize a modular reactor vessel.
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公开(公告)号：US11492559B2
公开(公告)日：2022-11-08
申请号：US16484978
申请日：2018-02-12
Applicant: Magema Technology, LLC
Inventor： Bertrand R. Klussmann , Michael J. Moore
IPC: C10G45/04 , C10G67/06 , C10G45/22 , C10G45/08 , C10G25/02 , C10G25/00 , B01D3/34 , B01J8/04 , C10G65/04 , C10L1/12 , C10L1/14 , C10L1/16 , B01D53/14 , C10G7/00 , C10G45/06 , C10L1/04 , C10G45/02 , C10G67/02 , B01J8/00 , B01J21/04 , B01J23/24 , B01J23/40 , B01J23/74 , C10G65/16 , B01J8/02 , C10G47/02 , C10G69/02
Abstract: A process and device for reducing the environmental contaminants in a ISO 8217 compliant Feedstock Heavy Marine Fuel Oil, the process involving: mixing a quantity of the Feedstock Heavy Marine Fuel Oil with a quantity of Activating Gas mixture to give a feedstock mixture; contacting the feedstock mixture with one or more catalysts to form a Process Mixture from the feedstock mixture; separating the Product Heavy Marine Fuel Oil liquid components of the Process Mixture from the gaseous components and by-product hydrocarbon components of the Process Mixture and, discharging the Product Heavy Marine Fuel Oil. The Product Heavy Marine Fuel Oil is compliant with ISO 821 7 for residual marine fuel oils and has a sulfur level has a maximum sulfur content (ISO 14596 or ISO 8754) between the range of 0.05% wt. to 0.5% wt. The Product Heavy Marine Fuel Oil can be used as or as a blending stock for an ISO 8217 compliant, IMO MARPOL Annex VI (revised) compliant low sulfur or ultralow sulfur heavy marine fuel oil.
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公开(公告)号：US20220348832A1
公开(公告)日：2022-11-03
申请号：US17245269
申请日：2021-04-30
Applicant: UOP LLC
Inventor： Yoga Ramamurthi Ayar , Rajesh Sivadasan , Richard Hoehn , Donald A. Eizenga
Abstract: A hydrocracking process for maximization of naphtha while producing base oil is disclosed. The hydrocracking process comprises hydrocracking a hydrocarbon feed stream in a hydrocracking unit in the presence of a hydrogen stream and a hydrocracking catalyst to produce a hydrocracked effluent stream. The hydrocracked effluent stream is separated in a separator to provide a vapor hydrocracked stream and a liquid hydrocracked stream. The liquid hydrocracked stream is fractionated to provide a naphtha stream, a kerosene stream, a diesel stream and a first unconverted oil stream. A recycle stream comprising a portion of the kerosene stream, a portion of the diesel stream, and a portion of the first unconverted oil stream is recycled to the hydrocracking unit to provide a second unconverted oil stream. A remaining portion of the first unconverted oil stream is withdrawn for base oil production.
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