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公开(公告)号:US10941349B2
公开(公告)日:2021-03-09
申请号:US16891203
申请日:2020-06-03
Applicant: Neste Oyj
Inventor: Juha Jakkula , Pekka Aalto , Vesa Niemi , Ulla Kiiski , Jouko Nikkonen , Seppo Mikkonen , Outi Piirainen
Abstract: The invention is directed to a fuel composition for diesel engines. The fuel composition comprises 0.1-99% by weight of a component or a mixture of components produced from biological raw material originating from plants and/or animals and/or fish. The fuel composition comprises 0-20% of components containing oxygen. Both components are mixed with diesel components based on crude oil and/or fractions from Fischer-Tropsch process.
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公开(公告)号:US20210062015A1
公开(公告)日:2021-03-04
申请号:US16958802
申请日:2018-12-20
Applicant: Neste Oyj
Inventor: Kati Sandberg , Virpi Rämö , Jenni Nortio , Anna Karvo
Abstract: A renewable solvent composition having a high i-paraffin content of at least 91.0 wt.-% and a boiling in a range of from 150° C. to 260° C. is disclosed. The solvent composition can provide a good balance between solvency power and cold properties and is usable in a broad application field.
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公开(公告)号:US10899983B1
公开(公告)日:2021-01-26
申请号:US16881293
申请日:2020-05-22
Applicant: ExxonMobil Research and Engineering Company
Inventor: Kenneth C. H. Kar , Sheryl B. Rubin-Pitel , Lisa M. Guay , Timothy J. Anderson , Shifang Luo , Marcia E. Dierolf
Abstract: Marine diesel fuel/fuel blending component compositions and fuel oil/fuel blending component compositions are provided that are derived from crude oils having high naphthenes to aromatics volume and/or weight ratios and a low sulfur content. In addition to having a high naphthenes to aromatics ratio, a low sulfur content, and a low but substantial content of aromatics, such fuels and/or fuel blending components can have a reduced or minimized carbon intensity relative to fuels derived from conventional sources. The unexpected ratio of naphthenes to aromatics contributes to the fuels and/or fuel blending components further having additional unexpected properties, including low density, low kinematic viscosity, and/or high energy density.
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公开(公告)号:US10850266B2
公开(公告)日:2020-12-01
申请号:US15714238
申请日:2017-09-25
Applicant: Mississippi State University
Inventor: Mark G. White , Shetian Liu
IPC: B01J29/48 , B01J29/78 , B01J29/08 , B01J23/28 , C10L3/12 , C10L1/08 , C10G2/00 , B01J37/02 , B01J29/16 , B01J29/076 , B01J29/26 , B01J29/03
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:US20200331824A1
公开(公告)日:2020-10-22
申请号:US16918324
申请日:2020-07-01
Applicant: Swift Fuels, LLC
Inventor: Chris D'Acosta , Jeffery Miller , Robert Hoch
Abstract: Disclosed herein are processes for the production of hydrocarbon fuel products from C2-5 alkanes. Methane is converted to ethylene in a methane thermal olefination reactor operating at a temperature of at least 900° C. and a pressure of at least 150 psig, and without a dehydrogenation catalyst or steam. C2-5 alkanes are converted to olefins in a C2-5 thermal olefination reactor operating at a temperature, pressure and space velocity to convert at least 80% of the alkanes to C2-5 olefins. The ethylene and C2-5 olefins are passed through an oligomerization reactor containing a zeolite catalyst and operating at a temperature, pressure and space velocity to crack, oligomerize and cyclize the olefins. In one aspect, methane in the effluent of the oligomerization reactor is recycled through the C2-5 thermal olefination reactor. Methods for the thermal olefination of methane are also disclosed.
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公开(公告)号:US10800976B2
公开(公告)日:2020-10-13
申请号:US16715871
申请日:2019-12-16
Applicant: NESTE OYJ
Inventor: Jukka Myllyoja , Pekka Aalto , Pekka Savolainen , Veli-Matti Purola , Ville Alopaeus , Johan Gronqvist
IPC: C10G3/00 , C10G45/58 , C07C5/22 , C10L1/08 , C10G45/62 , C10G45/64 , C10G65/04 , C07C5/27 , C10G45/02 , C07C1/24 , C07C5/03 , C07C7/10 , C07C7/12 , C07C7/13
Abstract: The invention relates to a process for the manufacture of diesel range hydrocarbons wherein a feed is hydrotreated in a hydrotreating step and isomerised in an isomerisation step, and a feed comprising fresh feed containing more than 5 wt % of free fatty acids and at least one diluting agent is hydrotreated at a reaction temperature of 200-400° C., in a hydrotreating reactor in the presence of catalyst, and the ratio of the diluting agent/fresh feed is 5-30:1.
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公开(公告)号:US20200291312A1
公开(公告)日:2020-09-17
申请号:US16820279
申请日:2020-03-16
Inventor: Ujjal Mukherjee , Essam Abdullah Al-Sayed , Pedro Santos , Kareemuddin Shaik , Theodorus Maesen , Mazin Tamimi , Julie Chabot , Ibrahim Abba , Kandasamy Sundaram , Sami Barnawi , Ronald Venner , Abdulrahman Akhras
Abstract: Processes herein may be used to thermally crack various hydrocarbon feeds, and may eliminate the refinery altogether while making the crude to chemicals process very flexible in terms of crude. In embodiments herein, crude is progressively separated into at least light and heavy fractions. Depending on the quality of the light and heavy fractions, these are routed to one of three upgrading operations, including a fixed bed hydroconversion unit, a fluidized catalytic conversion unit, or a residue hydrocracking unit that may utilize an ebullated bed reactor. Products from the upgrading operations may be used as feed to a steam cracker.
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公开(公告)号:US10774271B2
公开(公告)日:2020-09-15
申请号:US16501150
申请日:2019-02-26
Applicant: GREYROCK TECHNOLOGY, LLC
Inventor: Robert Schuetzle , Dennis Schuetzle
IPC: C10G2/00 , C10G45/02 , C10G45/62 , B01J23/89 , B01J35/00 , B01J35/02 , B01J35/10 , B01J37/02 , C10G45/00 , C10L1/08 , C10G7/00
Abstract: A unique process and catalyst is described that operates efficiently for the direct production of a high cetane diesel type fuel or diesel type blending stock from stochiometric mixtures of hydrogen and carbon monoxide. This invention allows for, but is not limited to, the economical and efficient production high quality diesel type fuels from small or distributed fuel production plants that have an annual production capacity of less than 10,000 barrels of product per day, by eliminating traditional wax upgrading processes. This catalytic process is ideal for distributed diesel fuel production plants such as gas to liquids production and other applications that require optimized economics based on supporting distributed feedstock resources.
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公开(公告)号:US10731085B2
公开(公告)日:2020-08-04
申请号:US16195037
申请日:2018-11-19
Applicant: UPM-KYMMENE CORPORATION
Inventor: Teemu Lindberg , Jaakko Nousiainen , Heli Laumola , Arto Rissanen
Abstract: The present invention provides a composition comprising 10-40 mass % of C8-30 linear alkanes, up to 20 mass % of C7-20 aromatic hydrocarbons, at least 90 mass % of which are monoaromatic, and no more than 1 mass % in total of oxygen-containing compounds; wherein the total amount of C8-30 alkanes in the composition is 50-95 mass %, and the total amount of C8-30 alkanes, C7-20 aromatic hydrocarbons and C8-30 cycloalkanes is at least 95 mass %; wherein the composition comprises 45-90 mass % in total of C8-30 cycloalkanes and C8-30 branched alkanes; and wherein the amounts are based on the mass of the composition. Also provided is a method of producing the composition comprising the step of hydroprocessing a biological feedstock using a catalyst and the step of fractionating the product of the hydroprocessing step.
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公开(公告)号:US10669490B2
公开(公告)日:2020-06-02
申请号:US15401400
申请日:2017-01-09
Applicant: DUPONT INDUSTRIAL BIOSCIENCES USA, LLC
Inventor: Hasan Dindi
Abstract: This disclosure relates to a process for producing diesel with reduced levels of sulfur. The process involves (a) providing a diesel feed comprising a diesel having a sulfur content in the range of about 20 to about 10,000 wppm; (b) feeding the diesel feed and a hydrogen rich gas to a reaction zone comprising a hydrotreating catalyst to produce a hydrotreated diesel effluent comprising diesel and hydrogen sulfide; and (c) removing hydrogen sulfide from the hydrotreated diesel effluent to produce a diesel product having a sulfur content no more than about 100 wppm; wherein hydrogen consumption in the reaction zone is in the range of about −150 to about 150 scf/bbl.
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