公开(公告)号：US20240336849A1

公开(公告)日：2024-10-10

申请号：US18627795

申请日：2024-04-05

申请人： 34MJ Pty Ltd

发明人： Morgan Hunter

IPC分类号： C10G3/00 ,  B01J19/00

CPC分类号： C10G3/44 ,  B01J19/008 ,  C10G2300/4012 ,  C10G2300/4068 ,  C10G2400/04

摘要： A mobile biodiesel manufacturing plant for continuously producing biodiesel from a triglyceride source and a method of continuously producing biodiesel from a triglyceride source in the mobile biodiesel manufacturing plant.

公开(公告)号：US12104120B2

公开(公告)日：2024-10-01

申请号：US18503850

申请日：2023-11-07

申请人： Anders Mokvist

发明人： Anders Mokvist

IPC分类号： C10G1/00 ,  B01D3/14 ,  C10L1/08

CPC分类号： C10G1/002 ,  B01D3/14 ,  C10L1/08 ,  C10G2300/1011 ,  C10G2400/04 ,  C10L2200/0469 ,  C10L2270/026 ,  C10L2290/24 ,  C10L2290/543

摘要： Disclosed herein is a method and system for converting biomass to biofuel, comprising a reaction apparatus including: a reaction tank configured to hold a process fluid; at least one mechanical rotating device comprising: a submergible chamber configured to operate within process, the submergible chamber having a first section including a first rotatable member and configured to receive biomass feedstock; a second section including a second rotatable member and configured to process biomass feedstock; and a third section including a third rotatable member and configured to treat the processed biomass feedstock effective to convert the processed biomass feedstock; a shaft in operable communication with each of the first, second, and third rotatable members for rotating said rotatable members about an axis; and a drive source for driving the shaft about said axis. Also disclosed herein are kits and methods for using the disclosed system to produce biofuel.

公开(公告)号：US12098334B2

公开(公告)日：2024-09-24

申请号：US18064845

申请日：2022-12-12

申请人： Duke Technologies, LLC

发明人： Michael D. Ackerson ,  Michael Steven Byars ,  Kyle Ackerson ,  John Coleman

IPC分类号： C10G69/02 ,  B01D17/02 ,  B01D19/00 ,  C10G3/00

CPC分类号： C10G69/02 ,  B01D17/0214 ,  B01D19/0005 ,  C10G3/40 ,  C10G2300/1003 ,  C10G2300/1011 ,  C10G2300/202 ,  C10G2300/205 ,  C10G2300/302 ,  C10G2300/308 ,  C10G2300/4006 ,  C10G2300/4018 ,  C10G2400/04

摘要： A non-petroleum or renewable feedstock containing oxygen and contaminants of metals, gums, and resins is treated by introducing the feedstock into a reactor at a flow velocity of at least 20 ft/sec. The feedstock is heated within the reactor and cooled to form a reduced-temperature reactor product. At least a portion of the reduced-temperature reactor product is feed into a hydroprocessing reactor containing a hydroprocessing catalyst to form a hydroprocessed product. The hydroprocessed product is cooled and non-condensable gases, metals and water are separated and removed to form a final product. The final product has an oxygen content that is 60% or less of that of the feedstock, and wherein the final product comprises 25 wt % or less any triglycerides, monoglycerides, diglycerides, free fatty acids, phosphatides, sterols, tocopherols, tocotrienols, or fatty alcohols, from 5 wt % to 30 wt % naphtha, and 50 wt % or more diesel.

公开(公告)号：US12077713B2

公开(公告)日：2024-09-03

申请号：US18449865

申请日：2023-08-15

申请人： Chevron Phillips Chemical Company LP

发明人： Ronald G. Abbott ,  Scott G. Morrison ,  Steven R. Horlacher ,  Jamie N. Sutherland ,  Bruce D. Murray ,  Jacob M. Hilbrich ,  Charles T. Polito

IPC分类号： C10B53/07 ,  C10G45/26 ,  C10G45/50 ,  C10G51/02 ,  C10G57/02

CPC分类号： C10B53/07 ,  C10G45/26 ,  C10G45/50 ,  C10G51/023 ,  C10G57/02 ,  C10G2300/1003 ,  C10G2400/04 ,  C10G2400/06 ,  C10G2400/20 ,  C10G2400/22 ,  C10G2400/28 ,  C10G2400/30

摘要： This disclosure relates to the production of chemicals and plastics using pyrolysis oil from the pyrolysis of plastic waste as a co-feedstock along with a petroleum-based, fossil fuel-based, or bio-based feedstock. In an aspect, the polymers and chemicals produced according to this disclosure can be certified under International Sustainability and Carbon Certification (ISCC) provisions as circular polymers and chemicals at any point along complex chemical reaction pathways. The use of a mass balance approach which attributes the pounds of pyrolyzed plastic products derived from pyrolysis oil to any output stream of a given unit has been developed, which permits ISCC certification agency approval.

公开(公告)号：US20240254401A1

公开(公告)日：2024-08-01

申请号：US18636450

申请日：2024-04-16

申请人： ThermoChem Recovery International, Inc.

发明人： Ravi Chandran ,  Dave G. Newport ,  Daniel A. Burciaga ,  Daniel Michael Leo ,  Justin Kevin Miller ,  Brian Christopher Attwood

IPC分类号： C10J3/84 ,  B01J19/00 ,  B01J19/24 ,  C01B3/34 ,  C01B3/50 ,  C07C29/151 ,  C07C41/01 ,  C10G2/00 ,  C10K1/00 ,  C10K3/06 ,  C10L1/02 ,  C10L1/06 ,  C10L1/08 ,  C12P7/06

CPC分类号： C10J3/84 ,  B01J19/0013 ,  B01J19/245 ,  C01B3/346 ,  C01B3/50 ,  C07C29/1518 ,  C07C41/01 ,  C10G2/344 ,  C10K1/004 ,  C10K1/007 ,  C10K3/06 ,  C10L1/023 ,  C10L1/026 ,  C10L1/06 ,  C10L1/08 ,  C12P7/06 ,  B01J2219/0004 ,  B01J2219/00157 ,  C01B2203/0233 ,  C01B2203/04 ,  C01B2203/06 ,  C01B2203/062 ,  C01B2203/0822 ,  C01B2203/1235 ,  C01B2203/84 ,  C10G2300/1022 ,  C10G2300/104 ,  C10G2300/1051 ,  C10G2300/1055 ,  C10G2300/4081 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10J2300/1628 ,  C10J2300/1643 ,  C10J2300/1656 ,  C10J2300/1659 ,  C10J2300/1665 ,  C10J2300/1671 ,  C10J2300/1823 ,  C10J2300/1853 ,  C10J2300/1884 ,  C10L2200/0423 ,  C10L2200/043 ,  C10L2200/0446 ,  C10L2270/023 ,  C10L2270/026 ,  C10L2270/04

摘要： A system for using carbonaceous material includes a steam reformer, a hydrocarbon reformer, and at least one gas-cleanup system. Also described are methods of producing liquid fuel and/or chemicals from carbonaceous material.

公开(公告)号：US20240247195A1

公开(公告)日：2024-07-25

申请号：US18417145

申请日：2024-01-19

申请人： UOP LLC

发明人： Ashish Mathur ,  Debanjan Chakrabarti ,  Jeannie Mee Blommel ,  Joel S. Paustian ,  Manuela Serban

IPC分类号： C10G69/12

CPC分类号： C10G69/126 ,  C10G2300/1092 ,  C10G2300/4081 ,  C10G2400/04 ,  C10G2400/08

摘要： A process for oligomerizing olefins to distillate fuels which oligomerizes a recycle olefin stream with a charge olefin stream in a first-stage oligomerization reactor. The first-stage oligomerate is oligomerized in a second-stage oligomerzation reactor to provide a second-stage oligomerate stream. The second-stage oligomer stream is hydrogenated to produce fuels. A stripping column is used to prepare the hydrogenated fuel streams for fractionation.

公开(公告)号：US20240150662A1

公开(公告)日：2024-05-09

申请号：US18417569

申请日：2024-01-19

申请人： Magema Technology LLC

发明人： Michael Joseph Moore ,  Bertrand Ray Klussmann ,  Carter James White

IPC分类号： C10G45/04 ,  B01D3/34 ,  B01D53/14 ,  B01J8/00 ,  B01J8/02 ,  B01J8/04 ,  B01J21/04 ,  B01J23/24 ,  B01J23/40 ,  B01J23/74 ,  C10G7/00 ,  C10G25/00 ,  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 ,  C10L1/16

CPC分类号： 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 ,  C10G2300/1037 ,  C10G2300/1044 ,  C10G2300/1048 ,  C10G2300/1059 ,  C10G2300/107 ,  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

摘要： A multi-stage process for transforming a high sulfur ISO 8217 compliant Feedstock Heavy Marine Fuel Oil involving a core desulfurizing process that produces a Product Heavy Marine Fuel Oil that can be used as a feedstock for subsequent refinery process such as anode grade coking, needle coking and fluid catalytic cracking. The Product Heavy Marine Fuel Oil exhibits multiple properties desirable as a feedstock for those processes including 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 is also disclosed.

公开(公告)号：US20240117262A1

公开(公告)日：2024-04-11

申请号：US18543032

申请日：2023-12-18

申请人： MARATHON PETROLEUM COMPANY LP

发明人： Richard L. Eller ,  Peg Broughton ,  V. Elijah Mullins ,  John R. Weber ,  Jeffrey A. Sexton

IPC分类号： C10L1/04 ,  C10G11/18 ,  C10G69/04 ,  C10L1/06 ,  C10L1/08 ,  C10L10/00

CPC分类号： 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

摘要： Fuel oil compositions, and methods for blending such fuel oil compositions, to enhance initial compatibility and longer term stability when such fuel oil compositions are blended to meet IMO 2020 low sulfur fuel oil requirements (ISO 8217). In one or more embodiments, asphaltenic resid base stocks are blended with high aromatic slurry oil to facilitate initial compatibility such that low sulfur cutter stocks, e.g., vacuum gas oil and/or cycle oil, may be further blended therein to cut sulfur content while maintaining longer term stability. These fuel oil compositions are economically advantageous when used as marine low sulfur fuel oils because greater concentrations of high viscosity resids are present in the final blend.

公开(公告)号：US11939535B2

公开(公告)日：2024-03-26

申请号：US17787783

申请日：2020-12-15

申请人： Petróleo Brasileiro S.A.—Petrobras

发明人： Jefferson Roberto Gomes ,  José Luiz Zotin ,  Anilza De Almeida Lyra Correa ,  Marcelo Edral Pacheco ,  Rodrigo Caetano Chistone

IPC分类号： C10G3/00 ,  B01J21/04 ,  B01J21/06 ,  B01J23/30 ,  B01J23/85 ,  B01J29/06 ,  B01J37/02 ,  C10G47/10

CPC分类号： C10G3/46 ,  B01J21/04 ,  B01J21/066 ,  B01J23/30 ,  B01J23/85 ,  B01J29/06 ,  B01J37/0201 ,  C10G3/50 ,  C10G47/10 ,  B01J2229/26 ,  C10G2300/1003 ,  C10G2300/1011 ,  C10G2400/02 ,  C10G2400/04

摘要： The present invention relates to a process for the conversion of plant oils, animal fats, waste food oils and carboxylic acids into renewable liquid fuels, such as bio-naphtha, bioQAV and renewable diesel, for use in combination with fossil fuels. The process is composed of two steps: hydrotreatment and hydrocracking. The effluent from the hydrotreatment step contains aromatics, olefins and compounds resulting from the polymerization of esters and acids. This is due to the use of partially reduced catalysts without the injection of a sulfiding agent and allows for the production of bioQAV of suitable quality for use in combination with fossil kerosene. Concurrently, the process generates, in addition to products in the distillation range of naphtha, kerosene and diesel, high molecular weight linear paraffins (up to 40 carbon atoms).

公开(公告)号：US20240093097A1

公开(公告)日：2024-03-21

申请号：US18445548

申请日：2023-10-06

申请人： Infinium Technology, LLC

发明人： Robert Schuetzle ,  Dennis Schuetzle ,  Anja Rumplecker Galloway ,  James Bucher

IPC分类号： C10G2/00 ,  C10K1/00 ,  C10L1/06 ,  C10L1/08 ,  C25B1/042 ,  C25B1/23 ,  C25B9/19 ,  C25B15/08

CPC分类号： C10G2/32 ,  C10K1/005 ,  C10L1/06 ,  C10L1/08 ,  C25B1/042 ,  C25B1/23 ,  C25B9/19 ,  C25B15/081 ,  C10G2300/307 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10L2200/0423 ,  C10L2200/043 ,  C10L2200/0446 ,  C10L2290/38 ,  C10L2290/46

摘要： Production of fuels from low carbon electricity and from carbon dioxide by the use of a solid oxide electrolysis cell (SOEC) and Fischer-Tropsch is shown. Fischer-Tropsch is an exothermic reaction that can be used to produce steam. Steam produced from the Liquid Fuel Production (LFP) reactor system, where the Fischer-Tropsch reaction occurs, is used as feed to the SOEC. The higher temperature steam improves the efficiency of the overall electrolysis system. The integration of the LFP steam improves the efficiency of the electrolysis because the heat of vaporization for the liquid water does not have to be supplied by the electrolyzer.