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公开(公告)号:US12187969B2
公开(公告)日:2025-01-07
申请号:US18151095
申请日:2023-01-06
Applicant: ThermoChem Recovery International, Inc.
Inventor: Ravi Chandran , Dave G. Newport , Daniel A. Burciaga , Daniel Michael Leo , Justin Kevin Miller , Brian Christopher Attwood
IPC: C01B3/34 , B01J19/00 , B01J19/24 , C01B3/50 , C07C29/151 , C07C41/01 , C10G2/00 , C10J3/84 , C10K1/00 , C10K3/06 , C10L1/02 , C10L1/06 , C10L1/08 , C12P7/06
Abstract: A method of producing liquid fuel and/or chemicals from a carbonaceous material entails combusting a conditioned syngas in pulse combustion heat exchangers of a steam reformer to help convert carbonaceous material into first reactor product gas which includes carbon monoxide, hydrogen, carbon dioxide and other gases. A portion of the first reactor product gas is transferred to a hydrogen reformer into which additional conditioned syngas is added and a reaction carried out to produce an improved syngas. The improved syngas is then subject to one or more gas clean-up steps to form a new conditioned syngas. A portion of the new conditioned syngas is recycled to be used as the conditioned syngas in the pulse combustion heat exchangers and in the hydrocarbon reformer. A system for carrying out the method include, a steam reformer, a hydrocarbon reformer, first and second gas-cleanup systems, a synthesis system and an upgrading system.
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公开(公告)号:US12157864B2
公开(公告)日:2024-12-03
申请号:US18333169
申请日:2023-06-12
Applicant: GENERAL AVIATION MODIFICATIONS, INC.
Inventor: George W Braly
Abstract: Unleaded aviation gasoline. An aviation gasoline fuel blend includes an unleaded aviation gasoline base fuel, with an effective amount of selected alkyl benzenes to improve the functional engine performance to avoid harmful detonation sufficient to meet or exceed selected standards for detonation performance requirements in full scale aircraft piston spark ignition engines designed for use with Grade 100LL avgas. Suitable alkylated benzenes may include a mixture of xylene isomers. Aromatic amines, such as m-toluidine, may also be added to increase MON. Base fuels may be a high quality aviation alkylate, or may be a commercial iso-octane, or a mixture of high quality aviation alkylate enhanced by iso-octane, or by commercial iso-octane mixtures, and may include iso-pentane or butane or both iso-pentane and butane in sufficient quantity to provide appropriate vapor pressure for the final fuel blend.
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公开(公告)号:US12146106B2
公开(公告)日:2024-11-19
申请号:US17658921
申请日:2022-04-12
Applicant: CHEVRON PHILLIPS CHEMICAL COMPANY LP
Inventor: Ronald G. Abbott , Bruce D. Murray , Scott G. Morrison , Bradley T. Price
IPC: C10G1/00 , C07C4/04 , C08F10/02 , C10B53/07 , C10B57/06 , C10G1/10 , C10G9/36 , C10G11/18 , C10L1/06 , C10L1/08 , C10L3/06
Abstract: Processes for using pyrolysis gas as a feedstock or a co-feedstock for making a variety of chemicals, for example, circular ethylene, circular ethylene polymers and copolymers, and other circular products. In these processes, pyrolysis reactor conditions can be selected to increase or optimized the production of pyrolysis gas over pyrolysis oil, and the pyrolysis gas which is usually used as fuel or flared can be fed downstream of the steam cracker furnace for economic use to form circular chemicals. Operating parameters of the pyrolysis unit may be adjusted to increase or decrease the proportion of pyrolysis gas relative to pyrolysis liquid as a function of their relative economic values.
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公开(公告)号:US20240286982A1
公开(公告)日:2024-08-29
申请号:US18571911
申请日:2022-06-28
Applicant: Topsoe A/S
Inventor: Magnus Zingler STUMMANN , Troels Dahlgaard STUMMANN
IPC: C07C29/151 , B01J6/00 , B01J19/24 , C01B3/34 , C07C1/12 , C10B53/00 , C10B53/02 , C10L1/06 , C25B1/042 , C25B15/08
CPC classification number: C07C29/1518 , B01J6/008 , B01J19/245 , C01B3/34 , C07C1/12 , C10B53/00 , C10B53/02 , C10L1/06 , C25B1/042 , C25B15/081 , C01B2203/0233 , C01B2203/061 , C01B2203/085 , C01B2203/1235 , C01B2203/1258 , C10L2200/0469 , C10L2200/0492 , C10L2290/02 , C10L2290/42
Abstract: Process for producing methane or methanol, said process comprising the steps of: i) conducting a solid renewable feedstock to a thermal decomposition step, this being a pyrolysis step or a hydrothermal liquefaction step, for producing: a first off-gas stream comprising hydrocarbons, a solid carbon stream, and optionally a first liquid oil stream; upgrading the first off-gas stream by conducting it to a hydro/deoxygenation (HDO/DO) step i.e. hydrodeoxygenation or deoxygenation step in which said HDO/DO step is conducted in the absence of steam, and a subsequent separation step, for generating water, a second liquid oil stream and an upgraded first off-gas stream; ii) conducting the first off-gas stream or the upgraded first off-gas stream to an olefin removal step, for generating a further upgraded first off-gas stream which is free of olefins; iii-1) conducting the first off-gas stream, or the upgraded first off-gas stream, or the further upgraded first off-gas stream, to a methanation step under the generation of steam for producing said methane; or iii-2) conducting the first off-gas stream, or the upgraded first off-gas stream, or the further upgraded first off-gas stream, to a steam reforming step for producing a methanol synthesis gas and subsequently conducting the methanol synthesis gas to a methanol synthesis step under the generation of steam for producing said methanol; iv) conducting steam, such as at least a portion of the steam generated in step iii-1) or iii-2), to an electrolysis step for producing an oxygen stream and a hydrogen stream; v) conducting at least a portion of the hydrogen stream from the electrolysis step to any of the: thermal decomposition step including HDO-step, olefin hydrogenation step, methanation step, methanol synthesis step, or combinations thereof.
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公开(公告)号:US20240279139A1
公开(公告)日:2024-08-22
申请号:US18591606
申请日:2024-02-29
Applicant: Swift Fuels, LLC
Inventor: Chris D'Acosta , Jeffery Miller , Kurtis Sluss
CPC classification number: C07C2/76 , C07C2/12 , C10G59/00 , C10L1/06 , C10L1/08 , C10G2300/1081 , C10G2300/4006 , C10G2300/4012 , C10G2300/4018 , C10G2300/4081 , C10G2400/02 , C10G2400/04 , C10L2200/0423 , C10L2200/0446 , C10L2270/023 , C10L2270/026 , C10L2290/06 , C10L2290/10
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:US12054679B2
公开(公告)日:2024-08-06
申请号:US17629087
申请日:2020-07-06
Applicant: IFP Energies nouvelles
Inventor: Sophie Couderc , Adrien Gomez , Clementina Lopez-Garcia , Philibert Leflaive , Damien Hudebine , Floriane Maldonado
CPC classification number: C10G65/04 , B01D3/143 , C10L1/06 , C10G2300/104 , C10G2300/1044 , C10G2300/202 , C10L2200/0423 , C10L2270/023 , C10L2290/543
Abstract: A process for the treatment of a gasoline containing sulfur compounds and olefins includes the following stages:
a) hydrodesulfurization in the presence of a catalyst having an oxide support and an active phase having a metal from group VIB and a metal from group VIII,
b) hydrodesulfurization at a higher temperature than that of stage a) and in the presence of a catalyst having an oxide support and an active phase with at least one metal from group VIII,
c) separation of H2S formed,
d) hydrodesulfurization at a low hydrogen/feedstock ratio and in the presence of a hydrodesulfurization catalyst having an oxide support and an active phase having a metal from group VIB and a metal from group VIII or an active phase with at least one metal from group VIII, and
e) further separation of H2S formed.-
公开(公告)号:US11964926B2
公开(公告)日:2024-04-23
申请号:US17954420
申请日:2022-09-28
Applicant: CHEVRON U.S.A. INC.
Inventor: Bong-Kyu Chang , Hye-Kyung Cho Timken , Huping Luo
CPC classification number: C07C2/60 , B01J31/0244 , C07C9/16 , C10L1/06 , C07C2531/02 , C10L2200/0423 , C10L2270/023
Abstract: A process for producing high octane alkylate is provided. The process involves reacting isobutane and ethylene using an ionic liquid catalyst. Reaction conditions can be chosen to assist in attaining, or to optimize, desirable alkylate yields and/or properties.
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公开(公告)号:US11920096B2
公开(公告)日:2024-03-05
申请号:US17832339
申请日:2022-06-03
Applicant: MARATHON PETROLEUM COMPANY LP
Inventor: Matthew T. Woodchick , V. Elijah Mullins , Peg Broughton
CPC classification number: C10L1/04 , C10G11/18 , C10G69/04 , C10L1/06 , C10L1/08 , C10L10/00 , C10G2300/107 , C10G2300/1077 , C10G2300/202 , C10G2300/205 , C10G2300/206 , C10G2300/207 , C10G2300/302 , C10G2300/304 , C10G2300/308 , C10G2400/04 , C10L2200/0263 , C10L2200/0438 , C10L2200/0446 , C10L2200/0461 , C10L2230/14 , C10L2270/026 , C10L2290/24 , C10L2290/46 , C10L2290/543 , C10L2290/547
Abstract: Low sulfur fuel oil blend compositions and methods of making such blend compositions to increase the stability and compatibility of LSFO blends having paraffinic resids that are blended with distillates and/or cracked stocks of higher asphaltenes and/or aromatics content. In one or more embodiments, distillates and/or cracked stocks that incrementally reduce the initial aromaticity of the distillate or cracked stock with the highest aromaticity are sequentially blended prior to resid addition. Such incremental reduction and sequential blending have been found to provide a resulting low sulfur fuel oil blend that is both compatible and stable.
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公开(公告)号:US11850566B2
公开(公告)日:2023-12-26
申请号:US17535263
申请日:2021-11-24
Applicant: Aircela Inc.
Inventor: Eric Dahlgren , Klaus S. Lackner
IPC: B01J19/24 , C10G3/00 , C10L1/06 , C10L1/08 , B01D53/62 , B01D53/78 , C25B1/04 , B01D53/96 , C25B15/08
CPC classification number: B01J19/245 , B01D53/62 , B01D53/78 , B01D53/965 , C10G3/00 , C10L1/06 , C10L1/08 , C25B1/04 , C25B15/081 , C25B15/087 , B01D2257/504 , B01J2219/0004 , C10G2400/02 , C10G2400/04 , C10G2400/08 , C10L2200/043 , C10L2200/0423 , C10L2200/0446
Abstract: A synthetic fuel production system and related techniques are disclosed. In accordance with some embodiments, the disclosed system may be configured to produce a liquid fuel using carbon dioxide extracted from the air and hydrogen generated from aqueous solutions by electrochemical means (e.g., water electrolysis). In production of the fuel, the disclosed system may be configured, in accordance with some embodiments, to react the carbon dioxide and hydrogen, for example, to form methanol. The disclosed system also may be configured, in accordance with some embodiments, to utilize one or more subsequent reaction steps to produce a given targeted set of hydrocarbons and partially oxidized hydrocarbons. For example, the disclosed system may be used to produce any one (or combination) of: ethanol; dimethyl ether; formic acid; formaldehyde; alkanes of various chain length; olefines; aliphatic and aromatic carbon compounds; and mixtures thereof, such as gasoline fuels, diesel fuels, and jet fuels.
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公开(公告)号:US11814595B1
公开(公告)日:2023-11-14
申请号:US17973172
申请日:2022-10-25
Inventor: Dario Lopez Pintor , John E. Dec
CPC classification number: C10L1/231 , C10L1/06 , C10L1/08 , C10L2200/0259 , C10L2270/023 , C10L2270/026
Abstract: According to various aspects, an additive for a hydrocarbon-based fuel has a formula (I), in which R1, R2, and R3 are each independently selected from —H, —CH3, or —CH2CH3, and at least one of R1, R2, or R3 is not —H. The additive improves an autoignition reactivity of the hydrocarbon-based fuel. The additive can be present in the fuel composition including the additive and the hydrocarbon-based fuel in an amount of 0.1% by volume to 5% by volume. The hydrocarbon-based fuel can comprise gasoline or diesel.
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