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公开(公告)号:US20240336854A1
公开(公告)日:2024-10-10
申请号:US18578697
申请日:2022-06-26
申请人: Iogen Corporation
发明人: Patrick J. Foody
CPC分类号: C10G49/007 , C01B3/34 , C01B2203/0233 , C01B2203/0405 , C01B2203/062 , C10G2300/1033
摘要: 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.
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公开(公告)号:US20240182798A1
公开(公告)日:2024-06-06
申请号:US18555143
申请日:2022-05-09
申请人: SHELL USA, INC.
CPC分类号: C10G49/002 , B01D29/17 , B01D39/2027 , B01D39/2068 , B01J8/0085 , B01J8/0453 , C10G2300/4006
摘要: 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.
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公开(公告)号:US20240181414A1
公开(公告)日:2024-06-06
申请号:US18556671
申请日:2022-04-21
申请人: CHEVRON U.S.A INC.
发明人: Steven Xuqi SONG , Matthew D. POLAND , Matthew D. FORMEL , David KASHEVAROFF , James France , Timothy D. EVANS
CPC分类号: B01J8/006 , B01D24/04 , C10G49/002
摘要: 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.
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公开(公告)号:US20230392085A1
公开(公告)日:2023-12-07
申请号:US18250047
申请日:2021-10-22
申请人: CHINA PETROLEUM & CHEMICAL CORPORATION , SINOPEC DALIAN RESEARCH INSTITUTE OF PETROLEUM AND PETROCHEMICALS CO., LTD.
发明人: Meng DAI , Shicai LI , Yang LI , Dahai XU , He DING , Guang CHEN , Han ZHANG , Jiawen ZHOU
CPC分类号: 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
摘要: 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.
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公开(公告)号:US20230347324A1
公开(公告)日:2023-11-02
申请号:US18344450
申请日:2023-06-29
申请人: Chevron U.S.A. Inc.
发明人: Xiaoying OUYANG , Viorel DUMA , Alexander KUPERMAN , Ibrahim UCKUNG , Theodorus Ludovicus Michael MAESEN , Axel BRAIT , Charles WILSON
IPC分类号: 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分类号: 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
摘要: 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.
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公开(公告)号:US20230295517A1
公开(公告)日:2023-09-21
申请号:US18006504
申请日:2021-09-17
IPC分类号: C10G2/00 , C01B3/16 , C10K3/02 , C25B15/08 , C10G3/00 , C10G49/00 , C10K1/00 , C10J3/00 , C01B3/34 , C10K1/08 , C25B1/04
CPC分类号: 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
摘要: 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.
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7.
公开(公告)号:US20220372384A1
公开(公告)日:2022-11-24
申请号:US17772602
申请日:2020-11-02
摘要: 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.
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公开(公告)号:US20220305398A1
公开(公告)日:2022-09-29
申请号:US17834339
申请日:2022-06-07
IPC分类号: 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
摘要: 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.
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公开(公告)号:US20220298441A1
公开(公告)日:2022-09-22
申请号:US17637210
申请日:2020-08-27
申请人: Iogen Corporation
发明人: Patrick J. Foody
摘要: A method of producing one or more fuels having a renewable content from a fuel production process that includes one or more processing steps wherein hydrogen is reacted with crude oil derived liquid hydrocarbon, where the hydrogen is produced by a plurality of hydrogen production units based on steam methane reforming. The method includes selecting one or more hydrogen production units from the plurality of hydrogen production units which have one or more hydrogen-producing characteristics, and allocating renewable methane such that a renewable fraction of feedstock for the selected hydrogen production units is greater than a renewable fraction of feedstock for other hydrogen production units. The selected hydrogen production units are selected to increase a yield of renewable content of one or more of the fuels produced by the fuel production process and/or reduce a carbon intensity of such fuels for a given quantity of renewable methane.
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公开(公告)号:US11345865B2
公开(公告)日:2022-05-31
申请号:US17042914
申请日:2019-06-06
发明人: Zhibing Zhang , Zheng Zhou , Weimin Meng , Feng Zhang , Lei Li , Baorong Wang , Gaodong Yang , Huaxun Luo , Guoqiang Yang , Hongzhou Tian , Yu Cao
摘要: The present invention relates to a micro-interface strengthening reaction system and method for heavy oil hydrogenation preparation of ship fuel, including a liquid phase feed unit, a gas phase feed unit, a micro-interface generator, a fixed-bed reactor and a separation tank. The present invention may reduce the pressure during the reaction by 10-80% while ensuring the efficiency of the reaction by breaking the gas to form micro-sized micro-bubbles and making the micro-bubbles mix with heavy oil to form an emulsion to increase the area between the gas and the liquid phase and to achieve the effect of enhancing mass transfer in a lower preset range. And, the present invention greatly enhances the mass transfer, so that the gas-liquid ratio can be greatly reduced. Also, the method of the present invention has low process severity, high production safety, low product cost per ton, and strong market competitiveness.
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