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公开(公告)号:US11021666B2
公开(公告)日:2021-06-01
申请号:US15386023
申请日:2016-12-21
Applicant: SHELL OIL COMPANY
Inventor: Cynthia Natalie Ginestra , Brice Nathaniel Dally , Joanna Margaret Bauldreay , Gregory Hemighaus
Abstract: By blending a quantity of synthetic cyclo-paraffinic kerosene fuel blending component comprising at least 99.5 mass % of carbon and hydrogen content and at least 50 mass % of cyclo-paraffin into kerosene base fuel, kerosene based-propulsion fuels can be upgraded to higher quality kerosene based-propulsion fuels such as jet fuel or rocket fuel to meet certain specification and/or increase volumetric energy content of the propulsion fuel.
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公开(公告)号:US10954452B2
公开(公告)日:2021-03-23
申请号:US16445113
申请日:2019-06-18
Applicant: Anellotech, Inc.
Inventor: Michael Tanzio , Charles M. Sorensen, Jr. , Marc E. Schneidkraut , Jeffrey P. Whiting
IPC: C07C209/86 , C07C209/08 , C10G7/00 , C07D209/08 , C07D307/79 , C07C37/70 , C10K1/08 , C10L1/02 , C10L1/04 , C10B57/06 , C10G1/08 , C10G1/10 , C10G3/00
Abstract: Methods of separating products from the catalytic fast pyrolysis of biomass are described. In a preferred method, a portion of the products from a pyrolysis reactor are recovered and separated using a quench system and solvent contacting system that employs materials produced in the pyrolysis process.
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公开(公告)号:US20210017459A1
公开(公告)日:2021-01-21
申请号:US17036441
申请日:2020-09-29
Applicant: MAWETAL LLC
Inventor: Mohammed Wohaibi , Tom F. Pruitt
Abstract: Methods are provided to prepare a low sulfur fuel from hydrocarbon sources, such as light tight oil and high sulfur fuel oil, often less desired by conventional refiners, who split crude into a wide range of differing products and may prefer presence of wide ranges (C3 or C5 to C20 or higher) of hydrocarbons. These fuels can be produced by separating feeds into untreated and treated streams, and then recombining them. Such fuels can also be formulated by combinations of light, middle and heavy range constituents in a selected manner as claimed. Not only low in sulfur, the fuels of this invention are also low in nitrogen and essentially metals free. Fuel use applications include on-board large marine transport vessels but also on-shore for large land based combustion gas turbines, boilers, fired heaters and transport vehicles and trains.
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公开(公告)号:US10883061B2
公开(公告)日:2021-01-05
申请号:US16409276
申请日:2019-05-10
Applicant: Calumet Specialty Products Partners, L.P.
Inventor: Anne B. Goldsmith , Edward Juno , John C. Burger , Indresh Mathur
Abstract: The present disclosure provides base aviation gasoline formulations. In addition, the present disclosure provides formulations in which one or more additives can optionally be added to the base aviation gasoline formulation to produce a finished aviation gasoline formulation.
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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:US10723621B2
公开(公告)日:2020-07-28
申请号:US16679837
申请日:2019-11-11
Applicant: Iogen Corporation
Inventor: Brian Foody
IPC: C01B3/34 , C10G65/02 , C10G45/02 , C10G47/00 , C10G65/12 , C12P5/02 , C10L3/08 , C10L3/10 , C07C5/02 , C12P5/00 , G06Q30/00 , C01B3/36 , C10G45/44 , C10L1/04 , G06Q50/06
Abstract: According to the present invention, organic material is converted to biogas through anaerobic digestion and the biogas is purified to yield a combustible fluid feedstock comprising methane. A fuel production facility utilizes or arranges to utilize combustible fluid feedstock to generate renewable hydrogen that is used to hydrogenate crude oil derived hydrocarbons in a process to make transportation or heating fuel. The renewable hydrogen is combined with crude oil derived hydrocarbons that have been desulfurized under conditions to hydrogenate the liquid hydrocarbon with the renewable hydrogen or alternatively, the renewable hydrogen can be added to a reactor operated so as to simultaneously desulfurize and hydrogenate the hydrocarbons. The present invention enables a party to receive a renewable fuel credit for the transportation or heating fuel.
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公开(公告)号:US20200224108A1
公开(公告)日:2020-07-16
申请号:US16681063
申请日:2019-11-12
Applicant: Magema 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 , 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 sulfur 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 contained within a frame work based on ISO 40 foot or ISO 20 foot container dimensions.
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公开(公告)号:US10704001B2
公开(公告)日:2020-07-07
申请号:US16025276
申请日:2018-07-02
Applicant: ExxonMobil Research and Engineering Company
Inventor: Kenneth Chi Hang Kar , Sheryl B. Rubin-Pitel , David T. Ferrughelli , Anthony S. Mennito , Teng Xu
Abstract: A first hydroprocessed product and a second hydroprocessed product produced from a multi-stage process for upgrading pyrolysis tar, such as steam cracker tar, are provided herein. Fuel blends including the first hydroprocessed product and/or the second hydroprocessed product are also provided herein as well as methods of lowering pour point of a gas oil using the first hydroprocessed product and the second hydroprocessed product.
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公开(公告)号:US10689309B1
公开(公告)日:2020-06-23
申请号:US16498386
申请日:2018-07-09
Applicant: TIANJIN UNIVERSITY
Inventor: Jijun Zou , Lun Pan , Xiangwen Zhang , Qingfa Wang
Abstract: A process for preparing a fused-ring alkane fuel, wherein the fused-ring alkane fuel has the following structure: wherein n is 1 or 2; R1, R2, R3, R4 and R5 are H or —CH3 or —CH2CH3; the fused-ring alkane fuel has a density of greater than 0.870 g/cm3, a freezing point of not higher than −50° C., and a net mass heat value of not less than 42.0 MJ/kg; the process for preparing a fused-ring alkane fuel, wherein the process includes steps of: (1) in a presence of ultraviolet light and a photocatalyst, a Diels-Alder cycloaddition reaction between a substituted or unsubstituted cyclic enone and a substituted or unsubstituted furan molecule occurs to produce a fuel precursor molecule: (2) the fuel precursor molecule obtained in the step (1) is subjected to hydrodeoxygenation to produce the fused-ring alkane fuel.
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公开(公告)号:US10647925B2
公开(公告)日:2020-05-12
申请号:US15390780
申请日:2016-12-27
Applicant: ExxonMobil Research and Engineering Company
Inventor: Sheryl B. Rubin-Pitel , Kenneth Kar , Kendall S. Fruchey
Abstract: Fuels and/or fuel blending components can be formed from hydroprocessing of high lift deasphalted oil. The high lift deasphalting can correspond to solvent deasphalting to produce a yield of deasphalted oil of at least 50 wt %, or at least 65 wt %, or at least 75 wt %. The resulting fuels and/or fuel blending components formed by hydroprocessing of the deasphalted oil can have unexpectedly high naphthene content and/or density. Additionally or alternately, deasphalted oil generated from high lift deasphalting represents a disadvantaged feed that can be converted into a fuel and/or fuel blending components with unexpected compositions. Additionally or alternately, the resulting fuels and/or fuel blending components can have unexpectedly beneficial cold flow properties, such as cloud point, pour point, and/or freeze point.
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