公开(公告)号：US12195677B2

公开(公告)日：2025-01-14

申请号：US17217585

申请日：2021-03-30

Applicant: Duke Technologies, LLC

Inventor： Michael D. Ackerson ,  Michael Steven Byars

IPC: C10G3/00 ,  C10G49/00 ,  C07C1/04

Abstract: A method of hydroprocessing is performed wherein non-petroleum feedstocks, such as those containing from about 10% or more olefinic compounds or heteroatom contaminants by weight, are treated in a first reaction zone to provide reaction products. The process involves introducing the feedstock along with diluents or a recycle and hydrogen in a first reaction zone and allowing the feed and hydrogen to react in a liquid phase within the first reaction zone to produce reaction products. The reaction products are cooled and/or water is removed from the reaction products. At least a portion of the cooled and/or separated reaction product are introduced as a feed along with hydrogen into a second reaction zone containing a hydroprocessing catalyst. The feed and hydrogen are allowed to react in a liquid phase within the second reaction zone to produce a second-reaction-zone reaction product.

公开(公告)号：US20240384181A1

公开(公告)日：2024-11-21

申请号：US18690673

申请日：2022-10-03

Applicant: ExxonMobil Chemical Patents Inc.

Inventor： Sundar Narayanan ,  Gaurav Agrawal ,  Teng Xu

IPC: C10G9/16 ,  C10G49/00 ,  C10G69/06

Abstract: The present disclosure generally relates to methods for reducing fouling in tar upgrading processes and to apparatus for carrying out such processes. In some embodiments, a method is provided that includes providing a first tar stream, combining the first tar stream with a utility fluid to form a first process stream having a viscosity lower than that of the first tar stream, and heating the first process stream in a pre-heater under liquid phase conditions without feeding molecular hydrogen gas into the pre-heater to form a second process stream exiting the pre-heater.

公开(公告)号：US20240336854A1

公开(公告)日：2024-10-10

申请号：US18578697

申请日：2022-06-26

Applicant: Iogen Corporation

Inventor： Patrick J. Foody

IPC: C10G49/00 ,  C01B3/34

CPC classification number: C10G49/007 ,  C01B3/34 ,  C01B2203/0233 ,  C01B2203/0405 ,  C01B2203/062 ,  C10G2300/1033

Abstract: Disclosed is a method for producing a fuel that has renewable content, the method comprising: providing renewable hydrogen sourced at least partially from causing renewable methane from a low carbon number fraction resulting from a conversion process to be fed, or co-fed with fossil material, to a hydrogen production unit to produce the renewable hydrogen, the feed to the conversion process being a carbon-containing renewable feedstock, the low carbon number fraction comprising carbon-containing molecules having 3 carbon atoms or less, the conversion process from which the hydrogen is sourced comprising a separation that fractionates the low carbon number fraction from a high carbon number fraction comprising carbon-containing molecules having 3 carbon atoms or more; and feeding the renewable hydrogen to at least part of a fossil fuel production facility to supply the renewable hydrogen thereto and produce the fuel that has renewable content.

公开(公告)号：US20240182798A1

公开(公告)日：2024-06-06

申请号：US18555143

申请日：2022-05-09

Applicant: SHELL USA, INC.

Inventor： Nicolaas VAN DIJK ,  Roy Léon Bemard HENKET ,  Julien SIGAUD

IPC: C10G49/00 ,  B01D29/17 ,  B01D39/20 ,  B01J8/00 ,  B01J8/04

CPC classification number: C10G49/002 ,  B01D29/17 ,  B01D39/2027 ,  B01D39/2068 ,  B01J8/0085 ,  B01J8/0453 ,  C10G2300/4006

Abstract: A process for hydroprocessing a renewable feedstock in a fixed-bed reactor system having at least one catalytic bed involves directing a downward flow of the renewable feedstock to a filtering zone having top-open interstitial portions to receive the downward flow and top-covered annular portions that are in fluid communication with a headspace between the filtering zone and a catalytic zone. The feedstock flows from the interstitial portions to the annular portions through a filtering material disposed between the interstitial portions and the annular portions, resulting in a filtered feedstock, which then flows to the catalytic zone. In the catalytic zone, filtered feedstock is reacted under hydroprocessing conditions sufficient to cause a reaction selected from the group consisting of hydrogenation, hydrodeoxygenation, hydrodenitrogenation, hydrodesulphurization, hydrodemetalation, hydrocracking, hydroisomerization, and combinations thereof.

公开(公告)号：US20240181414A1

公开(公告)日：2024-06-06

申请号：US18556671

申请日：2022-04-21

Applicant: CHEVRON U.S.A INC.

Inventor： Steven Xuqi SONG ,  Matthew D. POLAND ,  Matthew D. FORMEL ,  David KASHEVAROFF ,  James France ,  Timothy D. EVANS

IPC: B01J8/00 ,  B01D24/04 ,  C10G49/00

CPC classification number: B01J8/006 ,  B01D24/04 ,  C10G49/002

Abstract: A filtration device for a down-flow catalytic hydroprocessing reactor is disclosed. The filtration device may be used in the petroleum and chemical processing industries in catalytic reactions of hydrocarbonaceous feedstocks in the presence of hydrogen, at an elevated temperature and pressure, to remove contaminants from mixed gas and liquid feedstreams to reactor catalyst beds. The filtration device may be provided as a horizontal tray installation at the top of a reactor, whereby feedstream liquid is passed through a filtration media in a radially inward direction from the wall of the reactor to the center of the filtration device and thereafter to the reactor catalyst bed. Among the benefits provided are the minimization of scale and small/fine particulates that reach the catalyst bed below the device, reduced pressure drop through the reactor, even when the filter is completely fouled, and the potential for added catalyst volume due to the reduced need to use catalyst grading materials.

公开(公告)号：US20230392085A1

公开(公告)日：2023-12-07

申请号：US18250047

申请日：2021-10-22

Applicant: CHINA PETROLEUM & CHEMICAL CORPORATION ,  SINOPEC DALIAN RESEARCH INSTITUTE OF PETROLEUM AND PETROCHEMICALS CO., LTD.

Inventor： Meng DAI ,  Shicai LI ,  Yang LI ,  Dahai XU ,  He DING ,  Guang CHEN ,  Han ZHANG ,  Jiawen ZHOU

IPC: C10G49/00 ,  B01J8/04 ,  B01J8/02 ,  C10G65/16 ,  C10G65/08

CPC classification number: C10G49/002 ,  B01J8/0453 ,  B01J8/0492 ,  B01J8/025 ,  C10G65/16 ,  C10G65/08 ,  B01J2208/00823 ,  B01J2208/00893 ,  B01J2208/025 ,  B01J2208/00991 ,  C10G2400/04 ,  C10G2300/202 ,  C10G2300/4006 ,  C10G2300/4012 ,  C10G2300/4018 ,  C10G2300/4025 ,  C10G2300/4037 ,  C10G2300/1044 ,  C10G2300/1055 ,  C10G2300/1051 ,  C10G2300/30

Abstract: A multi-phase combination reaction system has at least one fixed bed hydrogenation reactor. The fixed bed hydrogenation reactor has, arranged from top to bottom, a first hydrogenation reaction area, a gas-liquid separation area, a second hydrogenation reaction area and a third hydrogenation reaction area. The gas-liquid separation area is provided with a raw oil inlet. A hydrogen inlet is provided between the second hydrogenation reaction area and the third hydrogenation reaction area. The system is capable of simultaneously obtaining two fractions in one hydrogenation reactor.

公开(公告)号：US20230347324A1

公开(公告)日：2023-11-02

申请号：US18344450

申请日：2023-06-29

Applicant: Chevron U.S.A. Inc.

Inventor： Xiaoying OUYANG ,  Viorel DUMA ,  Alexander KUPERMAN ,  Ibrahim UCKUNG ,  Theodorus Ludovicus Michael MAESEN ,  Axel BRAIT ,  Charles WILSON

IPC: B01J23/89 ,  B01J35/00 ,  B01J35/10 ,  B01J37/00 ,  B01J37/03 ,  B01J37/04 ,  B01J37/08 ,  B01J37/20 ,  C07C5/10 ,  C10G45/00 ,  C10G47/00 ,  C10G49/00

CPC classification number: B01J23/8993 ,  B01J35/0026 ,  B01J35/1019 ,  B01J35/1038 ,  B01J37/0045 ,  B01J37/031 ,  B01J37/04 ,  B01J37/08 ,  B01J37/20 ,  C07C5/10 ,  C10G45/00 ,  C10G47/00 ,  C10G49/00 ,  C10G2300/1055 ,  C10G2300/1074 ,  C10G2300/4006 ,  C10G2300/4012 ,  C10G2300/4018 ,  C10G2300/42 ,  C10G2300/70

Abstract: Bulk catalysts comprised of nickel, molybdenum, tungsten and titanium and methods for synthesizing bulk catalysts are provided. The catalysts are useful for hydroprocessing, particularly hydrodesulfurization and hydrodenitrogenation, of hydrocarbon feedstocks.

公开(公告)号：US20230295517A1

公开(公告)日：2023-09-21

申请号：US18006504

申请日：2021-09-17

Applicant: JOHNSON MATTHEY DAVY TECHNOLOGIES LIMITED

Inventor： Henry Arthur CLAXTON ,  Andrew James COE ,  Mark Joseph MCKENNA ,  Paul Robert TICEHURST

IPC: C10G2/00 ,  C01B3/16 ,  C10K3/02 ,  C25B15/08 ,  C10G3/00 ,  C10G49/00 ,  C10K1/00 ,  C10J3/00 ,  C01B3/34 ,  C10K1/08 ,  C25B1/04

CPC classification number: C10G2/32 ,  C01B3/16 ,  C01B3/34 ,  C10G3/50 ,  C10G49/007 ,  C10J3/00 ,  C10K1/005 ,  C10K1/08 ,  C10K3/026 ,  C25B1/04 ,  C25B15/081 ,  C01B2203/0415 ,  C01B2203/062 ,  C10G2300/1022 ,  C10G2300/4043 ,  C10G2300/4081 ,  C10J2300/0913 ,  C10J2300/0959 ,  C10J2300/1659 ,  C10J2300/1684

Abstract: A process for synthesising hydrocarbons is described comprising the steps of (a) making a synthesis gas comprising hydrogen, carbon monoxide and carbon dioxide from a feedstock in a synthesis gas generation unit, (b) removing carbon dioxide to produce a carbon dioxide stream and purified synthesis gas comprising hydrogen and carbon monoxide for synthesis gas in a Fischer-Tropsch hydrocarbon synthesis unit wherein (i) at least a portion of the FT water stream is fed to an electrolysis unit to provide an oxygen stream, which is fed to the synthesis gas generation unit. Carbon dioxide stream recovered from the carbon dioxide removal unit and a portion of the hydrogen stream produced by the electrolysis unit are fed to a reverse water-gas shift unit to produce a carbon monoxide stream, with carbon monoxide stream from the reverse water-gas shift unit fed to the Fischer-Tropsch hydrocarbon synthesis unit.

公开(公告)号：US20220372384A1

公开(公告)日：2022-11-24

申请号：US17772602

申请日：2020-11-02

Applicant: IFP Energies Nouvelles

Inventor： Wilfried WEISS ,  Isabelle MERDRIGNAC

IPC: C10G67/14 ,  C10G9/36 ,  C10G21/00 ,  C10G49/00 ,  C10G21/16 ,  C10G7/06 ,  C10G47/26

Abstract: The present invention relates to a process for producing olefins from a hydrocarbon feedstock 11 having a sulfur content of at least 0.1 weight %, an initial boiling point of at least 180° C. and a final boiling point of at least 600° C.

公开(公告)号：US20220305398A1

公开(公告)日：2022-09-29

申请号：US17834339

申请日：2022-06-07

Applicant: Energy Integration, Inc.

Inventor： Lynn Allen CRAWFORD ,  William Bryan SCHAFER, III

IPC: B01D1/28 ,  B01D1/26 ,  B01D3/14 ,  B01D3/00 ,  B01D1/00 ,  B01D9/00 ,  C07B31/00 ,  C07B33/00 ,  C07B35/02 ,  C07B35/04 ,  C07B35/08 ,  C07B37/08 ,  C07B37/10 ,  C10B55/00 ,  C10G7/00 ,  C10G9/00 ,  C10G11/00 ,  C10G31/06 ,  C10G45/00 ,  C10G47/00 ,  C10G49/00 ,  C10G50/00 ,  C10G51/00 ,  C10G53/00 ,  C10G55/00 ,  C10G57/00 ,  C10G59/00 ,  C10G61/00 ,  C10G63/00 ,  C10G65/00 ,  C10G67/00 ,  C10G69/00

Abstract: The present invention utilizes mechanical vapor compression and/or thermal vapor compression integrating compression loops across multiple process stages. A sequential network of compressors is utilized to increase the pressure and condensing temperature of the vapors within each process stage, as intra-vapor flow, and branching between process stages, as inter-vapor flow. Because the vapors available are shared among and between compressor stages, the number of compressors can be reduced, improving economics. Balancing vapor mass flow through incremental compressor stages which traverse multiple process stages by splitting vapors between compressor stages enables the overall vapor-compression system to be tailored to individual process energy requirements and to accommodate dynamic fluctuations in process conditions.