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公开(公告)号：US20240191147A1
公开(公告)日：2024-06-13
申请号：US18506264
申请日：2023-11-10
申请人： PHILLILPS 66 COMPANY
发明人： Jinfeng Lai , Leonard Nyadong
CPC分类号： C10G47/22 , C10G11/00 , C10G45/00 , G01N24/08 , G01N33/2835 , C10G2300/1059 , C10G2400/30
摘要： Processes for rapidly and accurately predicting the fouling potential of a heavy petroleum fraction in a commercial refinery, informing the selection of one or more interventions to prevent or decrease the rate of said fouling. The process utilizes several specialized 13C Nuclear Magnetic Resonance procedures to more accurately quantify tertiary and quaternary bridgehead aromatic carbon in the heavy petroleum fraction This permits more accurate calculation of a Condensation Index for the heavy petroleum fraction to more accurately predict fouling potential of the fraction. When the condensation index is at or above a threshold value, the process implements one or more responses to improve operational efficiency of the commercial refinery.
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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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3.发明授权公开(公告)号：US11788017B2
公开(公告)日：2023-10-17
申请号：US17856835
申请日：2022-07-01
CPC分类号： C10G45/04 , B01D53/1481 , C10G25/003 , C10L1/1608 , C10G2300/104 , C10G2300/1044 , C10G2300/202 , C10L2200/0263 , C10L2200/0438
摘要： A multi-stage process for reducing the Environmental Contaminants in a Feedstock Heavy Marine Fuel Oil that is compliant with ISO 8217: 2017 Table 2 as a residual marine fuel except for the concentration of Environmental Contaminants, the process involving a core hydrotreating process and either a pre-treating step or post-treating step to the core process that is selected from a) a sulfur absorption process unit; b) an oxidative desulfurizing process unit; and c) a microwave treatment process unit. The Product Heavy Marine Fuel Oil is compliant with ISO 8217 Table 2 as residual marine fuel and preferably has a sulfur level has a maximum sulfur content (ISO 14596 or ISO 8754) between the range of 0.05% wt. to 0.5% wt. A commercial scale process plant for conducting the process is disclosed.
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公开(公告)号：US11692146B1
公开(公告)日：2023-07-04
申请号：US17567440
申请日：2022-01-03
CPC分类号： C10G67/06 , C10G25/003 , C10G25/12 , C10G45/00 , C10G47/00 , C10G2300/107 , C10G2300/206 , C10G2300/301 , C10G2300/4025 , C10G2300/44 , C10G2300/708 , C10G2400/18 , C10G2400/20
摘要： A system for upgrading heavy hydrocarbon feeds, such as crude oil, include a hydrotreating unit, a hydrotreated effluent separation system, a solvent-assisted adsorption system, and a hydrocracking unit. Processes for upgrading heavy hydrocarbon feeds include hydrotreating the hydrocarbon feed to produce a hydrotreated effluent that includes asphaltenes, separating the hydrotreated effluent into a lesser boiling hydrotreated effluent and a greater boiling hydrotreated effluent comprising the asphaltenes, combining the greater boiling hydrotreated effluent with a light paraffin solvent to produce a combined stream, adsorbing the asphaltenes from the combined stream to produce an adsorption effluent, and hydrocracking the lesser boiling hydrotreated effluent and at least a portion of the adsorption effluent to produce a hydrocracked effluent with hydrocarbons boiling less than 180° C. The systems and processes increase the hydrocarbon conversion and yield of hydrocarbons boiling less than 180° C.
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公开(公告)号：US20220333026A1
公开(公告)日：2022-10-20
申请号：US17639871
申请日：2020-08-14
发明人： Stephen H. BROWN , Brenda A. RAICH , Samuel J. CADY , Anjaneya S. KOVVALI , Eric B. SHEN , Scott R. HORTON , Ashish B. MHADESHWAR , Aruna RAMKRISHNAN
摘要： An upgraded crude composition is provided, along with systems and methods for making such a composition. The upgraded crude composition can include an unexpectedly high percentage of vacuum gas oil boiling range components while having a reduce or minimized amount of components boiling above 593° C. (1100° F.). In some aspects, based in part on the hydroprocessing used to form the upgraded crude composition, the composition can include unexpectedly high contents of nitrogen. Still other unexpected features of the composition can include, but are not limited to, an unexpectedly high nitrogen content in the naphtha fraction; and an unexpected vacuum gas oil fraction including an unexpectedly high content of polynuclear aromatics, an unexpectedly high content of waxy, paraffinic compounds, and/or an unexpectedly high content of n-pentane asphaltenes.
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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：US11352579B2
公开(公告)日：2022-06-07
申请号：US16221742
申请日：2018-12-17
发明人： Daniel J. Eichelsdoerfer , Richard C. Dougherty , Charles L. Baker, Jr. , Rugved P. Pathare , Bryan E. Hagee
IPC分类号： C10M101/02 , C10G47/16 , C10G45/64 , C10G45/62 , C10G73/06 , C10G7/06 , B01J35/10 , B01J29/78 , C10G45/08 , C10G47/18 , C10G45/00 , C10G65/12 , C10G47/12 , C10N20/02 , C10N20/00 , C10N30/10 , C10N40/25
摘要： Disclosed are Group III base stocks comprising at least 30 wt % naphthenes, a viscosity index from 120 to 145; and a unique ratio of molecules with multi-ring naphthenes to single ring naphthenes (2R+N/1RN). A method for preparing the base stocks is also disclosed. Also disclosed is a lubricating oil having the base stock as a major component, and an additive as a minor component.
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公开(公告)号：US20220025283A1
公开(公告)日：2022-01-27
申请号：US17385402
申请日：2021-07-26
发明人： Suresh B. Koduru , Arun Arora
摘要： Integrated processes and systems for the production of distillate hydrocarbons and coke. The process may include feeding a hydrocarbon feedstock, comprising a residuum hydrocarbon fraction, to a residue hydrocracking reactor system to convert hydrocarbons therein, producing a hydrocracked effluent. The hydrocracked effluent may then be fed to a separation system, separating the hydrocracked effluent into one or more distillate hydrocarbon fractions and a vacuum residue fraction. The vacuum residue fraction may be fed to a coker system, converting the vacuum residue fraction into a coke product and a coker vapor effluent, recovering the coke product, and feeding the coker vapor effluent to the separation system. The one or more distillate hydrocarbon fractions are hydroprocessed to produce a hydroprocessed effluent, and the hydroprocessed effluent is separated into product distillate hydrocarbon fractions.
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公开(公告)号：US20220001341A1
公开(公告)日：2022-01-06
申请号：US17364182
申请日：2021-06-30
发明人： Pravesh Kumar , Ramesh Karumanchi , Sarvesh Kumar , Madhusudhan Sau , Gurpreet Singh Kapur , Sankara Sri Venkata Ramakumar
摘要： The invention relates to Quench box assembly comprising quench pipe and quench box, to mix quench gas and vapor-liquid effluent from previous catalyst bed to achieve equilibrium temperature before entering the next bed. The quench pipe is in the form of ring having aperture while quench box consists of swirling section and a mixing chamber. The swirling section consists of inclined baffles to provide swirling action to incoming stream and the turbulence created by the swirling action increases the heat transfer rate thus requiring the smaller reactor volume to attain equilibrium temperature. The perforated plate being open from all the sides allowing the liquid to flow uniformly from all directions thus providing uniform distribution on the distributor tray. Hence, eliminates the requirement of rough liquid distributor before the distribution tray.
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10.发明授权公开(公告)号：US11193144B2
公开(公告)日：2021-12-07
申请号：US16552622
申请日：2019-08-27
申请人： IOGEN CORPORATION
发明人： Patrick J. Foody
IPC分类号： C12P5/02 , C01B3/34 , C10G45/00 , C12P7/10 , C10G2/00 , C01B3/00 , C07C1/04 , C10J3/82 , C10L3/08 , C12P7/14 , C10J3/00
摘要： The present invention provides a process for producing one or more products for use as a transportation or heating fuel. In various embodiments the process comprises treating a cellulosic feedstock in one or more processing steps that release extractives from the feedstock. A solids-liquid separation is subsequently conducted on the process stream comprising the extractives and solids. An aqueous stream comprising one or more of the extractives may be fed to an anaerobic digester to produce crude biogas from which one or more impurities may optionally be removed. In various embodiments the process further comprises providing a solids stream to a thermal process. A product produced or derived from the thermal process may displace a product made from fossil fuel. One or more products obtained or derived from at least one of the foregoing process steps are provided for use as a transportation or heating fuel. In various embodiments the process enables advantaged fuel credit generation.
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