公开(公告)号：US11111446B2

公开(公告)日：2021-09-07

申请号：US15777338

申请日：2015-11-30

Applicant: CATECH TECHNOLOGY CO., LTD.

Inventor： Suan Li ,  Qingyu Deng ,  Kunpeng Wang

IPC: C10G47/36 ,  B01J8/22 ,  C10G1/08 ,  G05D23/00 ,  G05D23/12

Abstract: A temperature-controlling measure for a hydrogenation slurry bed reactor has three control points that are set from low to high: cold hydrogen is injected automatically when the system reaches control point 1; cold oil in injected automatically when the system reaches control point 2; each pressure relief is opened automatically when the system reaches control point 3. The pressure relief point is set before and/or after the circulation pump of the reactor if internal circulation is set in the reactor; the pressure relief point is set at the reactor bottom if the internal circulation is not set; at least one pressure relief valve is set at each pressure relief point.

公开(公告)号：US10829701B2

公开(公告)日：2020-11-10

申请号：US16404267

申请日：2019-05-06

Applicant: Petroraza SAS

Inventor： Jose Edgar Patiño ,  Farid Bernardo Cortés

IPC: C10G49/04 ,  B01J35/00 ,  B01J23/755 ,  B01J23/89 ,  E21B43/00 ,  B01J35/02 ,  B01J23/78 ,  B01J37/02 ,  B01J21/04 ,  B01J35/10 ,  C10G1/08 ,  C10G11/02 ,  C10G11/04

Abstract: Novel catalysts comprising nickel oxide nanoparticles supported on alumina nanoparticles, methods of their manufacture, heavy oil compositions contacted by these nanocatalysts and methods of their use are disclosed. The novel nanocatalysts are useful, inter alia, in the upgrading of heavy oil fractions or as aids in oil recovery from well reservoirs or downstream processing.

公开(公告)号：US10829696B2

公开(公告)日：2020-11-10

申请号：US16319878

申请日：2017-07-17

Applicant: SABIC Global Technologies B.V.

Inventor： Mohammad Javeed ,  Alexander Stanislaus ,  Abrar A. Hakeem ,  Girish Koripelly ,  Ravichander Narayanaswamy ,  Krishna Kumar Ramamurthy

IPC: C10G1/10 ,  C10G25/05 ,  C10G1/00 ,  C10G55/04 ,  C10G55/06 ,  B29B17/04 ,  C10G1/08 ,  C10B53/07 ,  C10G11/18 ,  C10G55/02 ,  C10K1/32 ,  C10K1/00 ,  B29K27/00

Abstract: A process for dechlorination of a hydrocarbon stream and/or a hydrocarbon stream precursor comprising introducing the hydrocarbon stream and/or hydrocarbon stream precursor, a first zeolitic catalyst, and a stripping gas to a devolatilization extruder (DE) to produce an extruder effluent, wherein the hydrocarbon stream and/or hydrocarbon stream precursor comprises one or more chloride compounds in an amount of equal to or greater than about 10 ppm chloride, based on the total weight of the hydrocarbon stream and/or hydrocarbon stream precursor, and wherein the extruder effluent comprises one or more chloride compounds in an amount of less than the chloride amount in the hydrocarbon stream and/or hydrocarbon stream precursor.

公开(公告)号：US10829695B2

公开(公告)日：2020-11-10

申请号：US15777856

申请日：2016-11-21

Applicant: SHELL OIL COMPANY

Inventor： Laxmi Narasimhan Chilkoor Soundararajan ,  Alan Anthony Del Paggio ,  Dhairya Dilip Mehta ,  Vikrant Nanasaheb Urade

IPC: C10G3/00 ,  C10G45/52 ,  C10G1/08 ,  C10G1/06 ,  C10G45/10 ,  C10G45/48 ,  C10G45/06 ,  C10G1/00 ,  C10G45/08 ,  C10G45/50

Abstract: A process for producing liquid hydrocarbon products from a biomass-containing feedstock and/or a biomass-derived feedstock is provided. The process comprises: a) contacting the feedstock with a hydropyrolysis catalyst composition and molecular hydrogen in a hydropyrolysis reactor vessel to produce a product stream comprising a deoxygenated hydrocarbon product, H2O, H2, CO2, CO, C1-C3 gases, char and catalyst fines; b) removing char and catalyst fines from said product stream; c) cooling the remaining product stream to a temperature of no more than 300° C.; and d) hydroconverting all or a portion of said deoxygenated hydrocarbon product in a hydroconversion reactor in the presence of one or more catalyst compositions suitable for the aromatic saturation of the deoxygenated hydrocarbon product and of the H2O, CO2, CO, H2, and C1-C3 gas generated in step a), to produce a product comprising C4+ hydrocarbon product, H2O, CO, CO2, and C1-C3 gases.

公开(公告)号：US10822562B2

公开(公告)日：2020-11-03

申请号：US16071232

申请日：2017-01-23

Applicant: ANELLOTECH, INC.

Inventor： Charles Sorensen

IPC: C10L1/16 ,  C10L1/06 ,  C10L1/12 ,  C10G1/00 ,  C07C5/10 ,  C10B53/02 ,  C10B57/06 ,  C10G1/08 ,  C10G45/54 ,  C10G45/56

Abstract: The present invention provides a catalytic fast pyrolysis process for the production of fuel blendstocks and chemicals. In addition, the invention provides compositions of renewable blendstocks, compositions of renewable fuel blends, and compositions of 100 percent renewable fuels compatible with gasoline specifications and regulations.

公开(公告)号：US20200299591A1

公开(公告)日：2020-09-24

申请号：US16899291

申请日：2020-06-11

Applicant: 1888711 ALBERTA INC.

Inventor： Roderick Michael Facey ,  Clayton Donald Allan

IPC: C10G11/18 ,  C10G3/00 ,  C10G1/08 ,  C10B53/02 ,  C10G70/04 ,  H01M8/06

Abstract: A method for thermal processing and catalytic cracking of a biomass to effect distillate oil recovery can include, particle size reduction. slurrying the biomass with a carrier fluid to create a reaction mixture, slurrying a catalyst with a carrier fluid to create a catalyst slurry, heating the reaction mixture and/or the catalyst slurry, and depolymerizing the reaction mixture with the catalyst. The reaction mixture can undergo distillation and fractionation to produce distillate fractions that include naphtha, kerosene, and diesel. In some embodiments, thermal processing and catalytic cracking includes vaporization of the biomass followed by distillation and fractionation. In some embodiments, a resulting distillate can be used as a carrier fluid. In some embodiments, the method can include desulfurization, dehydration, and/or decontamination.

公开(公告)号：US10751690B2

公开(公告)日：2020-08-25

申请号：US16560236

申请日：2019-09-04

Applicant: Licella Pty Ltd ,  Licella Fibre Fuels Pty Ltd ,  Ignite Resources Pty Ltd

Inventor： Robert Downie ,  Leonard James Humphreys ,  Thomas Maschmeyer ,  William Rowlands

IPC: B01J20/20 ,  C10L1/02 ,  B01J19/00 ,  B01J8/00 ,  C10G1/02 ,  C10G1/04 ,  C10G1/08

Abstract: The present invention relates generally to the generation of bio-products from organic matter feedstocks. More specifically, the present invention relates to improved methods for the hydrothermal/thermochemical conversion of lignocellulosic and/or fossilised organic feedstocks into biofuels (e.g. bio-oils) and/or chemical products (e.g. platform chemicals).

公开(公告)号：US10723956B2

公开(公告)日：2020-07-28

申请号：US16041110

申请日：2018-07-20

Applicant: 1888711 Alberta Inc.

Inventor： Roderick Michael Facey ,  Clayton Donald Allan

IPC: C10G11/18 ,  C10G3/00 ,  C10G1/08 ,  C10B53/02 ,  C10G70/04 ,  H01M8/06

Abstract: A method for thermal processing and catalytic cracking of a biomass to effect distillate oil recovery can include, particle size reduction. slurrying the biomass with a carrier fluid to create a reaction mixture, slurrying a catalyst with a carrier fluid to create a catalyst slurry, heating the reaction mixture and/or the catalyst slurry, and depolymerizing the reaction mixture with the catalyst. The reaction mixture can undergo distillation and fractionation to produce distillate fractions that include naphtha, kerosene, and diesel. In some embodiments, thermal processing and catalytic cracking includes vaporization of the biomass followed by distillation and fractionation. In some embodiments, a resulting distillate can be used as a carrier fluid. In some embodiments, the method can include desulfurization, dehydration, and/or decontamination.

公开(公告)号：US20200165527A1

公开(公告)日：2020-05-28

申请号：US16631697

申请日：2017-07-27

Applicant: Anellotech, Inc.

Inventor： Romina DIGNE ,  Cristina RUIZ MARTINEZ ,  Alexandre Bernard PAGOT ,  Marc François Philippe JACQUIN ,  Frédéric Jean-Michel FEUGNET ,  Charles Mitchel SORENSEN

IPC: C10G1/00 ,  C10G1/08 ,  C10G5/04

Abstract: A process comprising separating from a biomass catalytic pyrolysis process effluent, a naphthalene-rich oil phase, a phenolic oil and a vapor phase containing off gas, water and BTX, whereby said vapor phase can be condensed to separate liquid water and liquid hydrocarbons from gaseous off gas and BTX.

公开(公告)号：US20200095505A1

公开(公告)日：2020-03-26

申请号：US16473040

申请日：2017-06-13

Applicant: TGE IP LLC

Inventor： Christian KOCH

IPC: C10G1/00 ,  C10G1/02 ,  C10G1/08 ,  C10G11/22 ,  B01J10/00 ,  B01J19/00 ,  B01J19/18 ,  B01D3/14

Abstract: A method or catalytic compressed air conversion of hydrocarbonaceous substances to oil has the steps of: providing a hydrocarbonaceous substance and a catalyst oil in a mixing turbine, mixing the catalyst oil with the hydrocarbonaceous substance to give a mixture, where the step of mixing comprises producing heat for a catalytic oxidation in the mixing turbine, providing the distillation device downstream of the mixing turbine, removing liquid constituents of the mixture into the distillation device, distilling the liquid constituents, and collecting oil and water, and is characterized in that the step of mixing comprises introducing oxygen into the mixing turbine. An apparatus with which this method can be employed has a mixing turbine comprising a first feed for a catalyst oil and a hydrocarbonaceous substance and an outlet for liquid constituents after a catalytic oxidation. In addition, such an apparatus comprises a distillation device for distilling the liquid constituents led out of the mixing turbine and a collecting device for collecting oil and water separated out from the distillation device, wherein the mixing turbine has a second feed for oxygen.