-
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.
-
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.
-
公开(公告)号:US11807823B2
公开(公告)日:2023-11-07
申请号:US17803254
申请日:2022-04-04
Applicant: Fuel Blending Solutions, LLC
Inventor: Robert Schuetzle , Dennis Schuetzle
CPC classification number: C10L1/08 , C01B3/34 , C10G2/30 , C10G3/00 , C10J3/82 , C10K3/006 , C10L1/02 , C10L1/04 , C01B2203/0216 , C01B2203/0233 , C01B2203/0244 , C01B2203/04 , C01B2203/048 , C01B2203/0485 , C01B2203/061 , C01B2203/062 , C10L2200/0492 , C10L2290/04 , C10L2290/24 , C10L2290/42 , Y02E10/00 , Y02E10/20 , Y02E50/00 , Y02E50/10 , Y02E50/30 , Y02E60/00 , Y02E70/00 , Y02P20/145 , Y02P30/00 , Y02P30/20
Abstract: The present invention provides a blended fuel and methods for producing the blended fuel, wherein a low carbon fuel derived from a renewable resource such as biomass, is blended with a traditional, petroleum derived fuel. A blended fuel which includes greater than 10% by volume of low carbon fuel has an overall improved lifecycle greenhouse gas content of about 5% or more compared to the petroleum derived fuel. Also, blending of the low carbon fuel to the traditional, petroleum fuel improves various engine performance characteristics of the traditional fuel.
-
公开(公告)号:US11795408B2
公开(公告)日:2023-10-24
申请号:US17678508
申请日:2022-02-23
Applicant: Neste Oyj
Inventor: Markku Kuronen , Ulla Kiiski
CPC classification number: C10L1/023 , C10L1/026 , C10L1/06 , C10L1/08 , C10L2200/0446 , C10L2200/0469 , C10L2270/026 , Y02E50/10 , Y02P30/20
Abstract: Methods of making a diesel fuel blend having enhanced cold properties; methods of lowering the cloud point of a mineral middle distillate fuel; and diesel fuel blends including a blend of a renewable fuel and a mineral middle distillate fuel.
-
公开(公告)号:US11697778B2
公开(公告)日:2023-07-11
申请号:US17397292
申请日:2021-08-09
Inventor: Ujjal Mukherjee , Kareemuddin Shaik , Pedro Santos , Essam Abdullah Al-Sayed , Theodorus Maesen , Mazin Tamimi , Julie Chabot , Ibrahim Abba , Kandasamy Sundaram , Sami Barnawi , Ronald Venner
IPC: C10G69/06 , C10G9/36 , B01J19/24 , C10L1/08 , C10G45/26 , C10G45/32 , C10G45/44 , C10G49/22 , C10G65/12 , C10G47/30 , C10G49/02 , C10G21/00 , C10G47/26 , C10G55/04 , B01D3/06 , B01D19/00
CPC classification number: C10G69/06 , B01J19/245 , C10G9/36 , C10G21/003 , C10G45/26 , C10G45/32 , C10G45/44 , C10G47/26 , C10G47/30 , C10G49/02 , C10G49/22 , C10G55/04 , C10G65/12 , C10L1/08 , B01D3/06 , B01D19/0057 , B01J2219/0004 , C10G2300/1044 , C10G2300/1048 , C10G2300/202 , C10G2300/205 , C10G2300/206 , C10G2300/301 , C10G2300/302 , C10G2300/308 , C10G2300/40 , C10G2300/4006 , C10G2300/4081 , C10G2300/807 , C10G2400/20 , C10G2400/22 , C10G2400/30
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.
-
公开(公告)号:US20230203381A1
公开(公告)日:2023-06-29
申请号:US18083650
申请日:2022-12-19
Applicant: UPM-KYMMENE CORPORATION
Inventor: Andrea GUTIERREZ , Roel WESTERHOF , Sascha KERSTEN , Bert HEESINK , Pekka JOKELA
CPC classification number: C10G1/042 , C10G1/002 , C10L1/08 , C10G2300/4006 , C10G2300/4012 , C10L2270/026 , C10G2400/04 , C10G2400/08 , C10G2300/1003 , C10G2300/202 , C10L2200/0469 , C10L2290/06
Abstract: The disclosure relates to a process for converting lignin (10) to renewable product (80), wherein the process comprises the following steps; mixing (100) lignin (10) with aqueous solution (20) to obtain a mixture (30); heating (110) the mixture (30) of step (a) to a temperature between 290 and 350° C., under a pressure from 70 to 165 bar, to obtain a first product mix (40); separating aqueous phase (53) and oil phase (50), and optionally gas (51) and solids (52), of the first product mix (40) of step (b); and heating (130) the oil phase (50) of step (c) and solvent (60) to obtain a second product mix (70). The second product mix (70) can be used as such, it can be directed to separation (140) or it can be upgraded. The obtained liquid renewable product is suitable as chemicals, fuel, fuel components or feedstock for fuel production.
-
公开(公告)号:US11685869B2
公开(公告)日:2023-06-27
申请号:US17492324
申请日:2021-10-01
Applicant: Emerging Fuels Technology, Inc.
Inventor: Kenneth L. Agee , Jennifer Parker
CPC classification number: C10G67/02 , C10L1/08 , C10G2300/1022 , C10G2400/08 , C10L2270/04
Abstract: A method to produce a fuel product such as jet fuel, diesel or single battlefield fuel from a Fischer Tropsch syncrude comprising the steps of: 1) Separating the HFTL product from the reactor effluent gasses at reactor temperature and partially cooling the reactor effluent gas before transferring it to the enhanced hot separator; 2) enhancing the hot separator downstream of the Fischer Tropsch reactor with trays or packing and also adding reflux of the LFTL product, to improve separation efficiency and substantially reduce the C16+ portion of the hydrocarbons in the LFTL product; 3) combining the HFTL and MFTL product to from a combined HFTL product and further processing the combined HFTL in a hydroprocessing reactor that has a stacked bed with a layer of hydrocracking catalyst to crack the waxy C20+ hydrocarbons and a layer of hydroisomerization catalyst to isomerize the light fraction to increase the iso to n-paraffin ratio of the hydroprocessed product; 4) the LFTL product that is not recycled to the hot separator as reflux, bypasses the hydroprocessing reactor and is blended with the hydroprocessed product before distillation; and 5) the combined raw LFTL product and the hydroprocessed product is distilled to make naphtha, a fuel product, and a baseoil product. The method may be modified to make a single fuel product, preferably a jet fuel product.
-
公开(公告)号:US20230193143A1
公开(公告)日:2023-06-22
申请号:US17985604
申请日:2022-11-11
Applicant: UOP LLC
Inventor: Stanley Joseph Frey , Haiyan Wang , Andrea G. Bozzano
IPC: C10G45/64 , C10G3/00 , C10G7/00 , B01J29/85 , B01J37/00 , B01J21/04 , B01J23/30 , B01J23/888 , B01J37/02 , C10G47/34 , C10G69/04 , C10L1/08
CPC classification number: C10G45/64 , C10G3/42 , C10G3/50 , C10G7/00 , B01J29/85 , B01J37/0009 , B01J21/04 , B01J23/30 , B01J23/888 , B01J37/0201 , C10G47/34 , C10G69/04 , C10L1/08 , C10G2400/08 , C10G2300/304 , C10G2300/301 , C10G2300/308 , B01J2229/18 , C10G2300/4081 , C10G2300/70 , C10G2300/1011 , C10L2200/0469 , C10L2290/10 , C10L2290/543
Abstract: A new catalyst hydroisomerizes C18 paraffins from fatty acids to a high degree to produce a composition with acceptable freeze point which retains 18 carbon atoms in the hydrocarbon molecule for jet fuel. We have discovered a fuel composition comprising at least 14 wt % hydrocarbon molecules having at least 18 carbon atoms and a freeze point not higher than −40° C. The composition also may exhibit a exhibiting a final boiling point of no more than 300° C. The hydroisomerization process can be once through or a portion of the product diesel stream may be selectively hydrocracked or recycled to hydroisomerization to obtain a fuel composition that meets jet fuel specifications.
-
29.
公开(公告)号:US20230159837A1
公开(公告)日:2023-05-25
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: C10J3/84 , C07C41/01 , C07C29/151 , C10K3/06 , C10K1/00 , C10L1/02 , C10L1/06 , C10L1/08 , C10G2/00 , C01B3/34 , C01B3/50 , C12P7/06 , B01J19/24 , B01J19/00
CPC classification number: C10J3/84 , C07C41/01 , C07C29/1518 , C10K3/06 , C10K1/007 , C10K1/004 , C10L1/023 , C10L1/026 , C10L1/06 , C10L1/08 , C10G2/344 , C01B3/346 , C01B3/50 , C12P7/06 , B01J19/245 , B01J19/0013 , C10L2200/043 , C10L2270/04 , C10G2300/1051 , C10G2400/08 , C10L2200/0423 , C10L2270/023 , C10G2300/104 , C10G2400/02 , C10L2200/0446 , C10L2270/026 , C10G2300/1055 , C10G2400/04 , C10G2300/1022 , C10J2300/1823 , C10J2300/1853 , C10J2300/1884 , C10G2300/4081 , C10J2300/1656 , C10J2300/1665 , C10J2300/1659 , C10J2300/1671 , C10J2300/1643 , B01J2219/00157 , B01J2219/0004 , C01B2203/0233 , C01B2203/04 , C01B2203/062 , C01B2203/06 , C01B2203/84 , C01B2203/1235 , C01B2203/0822 , C10J2300/1628
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.
-
30.
公开(公告)号:US11653675B2
公开(公告)日:2023-05-23
申请号:US17448096
申请日:2021-09-20
Applicant: Novita Nutrition, LLC
Inventor: Keith Bruinsma , Donald Endres , Steven J. Furcich
IPC: C11B1/10 , C10G3/00 , A23K10/38 , B01D11/02 , C11C1/02 , C11C3/00 , A23J1/12 , C11B9/00 , C10L1/02 , C11C3/10 , C10L1/08 , C07C67/035 , C11B1/02 , C07C67/02
CPC classification number: C11B1/10 , A23K10/38 , B01D11/0288 , C10G3/50 , C11C1/025 , C11C3/00 , A23J1/12 , C07C67/02 , C07C67/035 , C10L1/026 , C10L1/08 , C10L2200/0469 , C10L2200/0476 , C10L2270/026 , C10L2290/26 , C10L2290/544 , C11B1/02 , C11B1/025 , C11B9/0003 , C11C3/003 , C11C3/10 , Y02E50/10 , Y02P30/20 , Y02P60/87
Abstract: A process for extraction of crude oil from distillers dried grain solubles and/or distillers dried grains using a solvent extraction process and producing corn distillers meal that may be used as an animal feed supplement is disclosed. The corn distillers meal may be used as a crude protein supplement for use in a livestock feed diet, poultry feed diet, aquatic feed diet or the like. The solvent extracted crude oil may be suitable for other processes, including oleochemical processing for personal care and home care products, biodiesel production, and/or renewable diesel production from hydro-treating the extracted oil to make green diesel fuel.
-
-
-
-
-
-
-
-
-