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公开(公告)号：US11560520B2
公开(公告)日：2023-01-24
申请号：US16103891
申请日：2018-08-14
IPC分类号： C10G45/02 , C10G45/04 , C10G67/06 , C10G45/22 , C10G45/08 , C10G25/02 , C10G25/00 , B01D3/34 , B01J8/04 , C10G65/04 , C10L1/12 , C10L1/14 , C10L1/16 , B01D53/14 , C10G7/00 , C10G45/06 , C10L1/04 , C10G67/02 , B01J8/00 , B01J21/04 , B01J23/24 , B01J23/40 , B01J23/74 , C10G65/16 , B01J8/02 , C10G47/02 , C10G69/02
摘要： A multi-stage process for reducing the environmental contaminants in an ISO8217 compliant Feedstock Heavy Marine Fuel Oil involving a core desulfurizing process and a Detrimental Solids removal unit as either a pre-treating step or post-treating step to the core process. The Product Heavy Marine Fuel Oil complies with ISO 8217 for residual marine fuel oils and has a sulfur level has a maximum sulfur content (ISO 14596 or ISO 8754) between the range of 0.05 mass % to 1.0 mass and a Detrimental Solids content less than 60 mg/kg. A process plant for conducting the process is also disclosed.
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公开(公告)号：US11530360B2
公开(公告)日：2022-12-20
申请号：US16681093
申请日：2019-11-12
IPC分类号： C10G65/16 , C10G69/02 , C10G45/02 , C10G45/22 , C10G65/04 , C10G67/02 , B01J23/24 , B01J23/40 , B01J23/74 , B01J8/02 , C10G47/02 , C10G45/04 , C10G67/06 , C10G45/08 , C10G25/02 , C10G25/00 , B01D3/34 , B01J8/04 , C10L1/12 , C10L1/14 , C10L1/16 , B01D53/14 , C10G7/00 , C10G45/06 , C10L1/04 , B01J8/00 , B01J21/04
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.
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公开(公告)号：US20220372382A1
公开(公告)日：2022-11-24
申请号：US17663530
申请日：2022-05-16
发明人： Pushkar VARSHNEY , Saravanan SUBRAMANI , Reshmi MANNA , Madhusudan SAU , Gurpreet Kapur SINGH , Sankara Sri Venkata RAMAKUMAR
摘要： The present invention is related to the isomerization process in which a light naphtha stream comprising of paraffinic (mono and single branched), naphthenic and aromatic hydrocarbons in the range of C5-C7 is contacted with the solid catalyst in multiple reaction zones and in presence of hydrogen to produce high octane gasoline predominantly comprising of paraffins (single and di-branched) and naphthenes. The process scheme comprises of more than one isomerization reaction section operating at different temperatures and other operating conditions. The catalyst employed in these reaction sections is a high coordination sulfated mixed metal oxide catalyst which contains at least one noble metal and sulfated zirconia in addition to the other components. The process of the present invention also comprises more than one fractionation section and recycling of a particular stream to the reaction zone for improving the isomerization of light naphtha.
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公开(公告)号：US11478724B2
公开(公告)日：2022-10-25
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：US20220333020A1
公开(公告)日：2022-10-20
申请号：US17856853
申请日：2022-07-01
IPC分类号： C10G45/04 , C10G67/06 , C10G45/22 , C10G45/08 , C10G25/02 , C10G25/00 , B01D3/34 , B01J8/04 , C10G65/04 , C10L1/12 , C10L1/14 , C10L1/16 , B01D53/14 , C10G7/00 , C10G45/06 , C10L1/04 , C10G45/02 , C10G67/02 , B01J8/00 , B01J21/04 , B01J23/24 , B01J23/40 , B01J23/74 , C10G65/16 , B01J8/02 , C10G47/02 , C10G69/02
摘要： A multi-stage process for the production of a Product Heavy Marine Fuel Oil compliant with ISO 8217: 2017 as a Table 2 residual marine fuel from a high sulfur Feedstock Heavy Marine Fuel Oil compliant with ISO 8217: 2017 as a Table 2 residual marine fuel except for the sulfur level, involving hydrotreating under reactive distillation conditions in a Reaction System composed of one or more reaction vessels. The reactive distillation conditions allow more than 75% by mass of the Process Mixture to exit the bottom of the reaction vessel as Product Heavy Marine Fuel Oil. The Product Heavy Marine Fuel Oil has a maximum sulfur content (ISO 14596 or ISO 8754) less than 0.5 mass %. A process plant for conducting the process for conducting the process is disclosed.
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公开(公告)号：US20220325191A1
公开(公告)日：2022-10-13
申请号：US17628687
申请日：2020-07-06
发明人： Sophie COUDERC , Adrien GOMEZ , Clementina LOPEZ GARCIA , Philibert LEFLAIVE , Damien HUDEBINE , Floriane MALDONADO
摘要： The present invention concerns a method for processing a petrol containing sulfur and olefin compounds, comprising the following steps: a) a step of hydrodesulfurisation in the presence of a catalyst comprising an oxide support and an active phase comprising a metal from group VIB and a metal from group VIII, b) a step of separating the H2S formed, c) a step of hydrodesulfurisation at a higher temperature than that of step a), with a hydrogen/feedstock ratio less than that of step a), and in the presence of a hydrodesulfurisation catalyst comprising an oxide support and an active phase consisting of at least one metal from group VIII, d) a step of separating the H2S formed.
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公开(公告)号：US20220204873A1
公开(公告)日：2022-06-30
申请号：US17137928
申请日：2020-12-30
申请人： Chevron U.S.A. Inc.
发明人： Ling Jiao , Bi-Zeng Zhan , Don Bushee , Theodorus Ludovicus Michael Maesen , Hye-Kyung Timken , Richard Dutta , Jay Parekh
摘要： Provided is a hydrocracking process with a recycle loop for converting a petroleum feed to lower boiling products, which process comprises reacting a stream over a non-zeolite noble metal catalyst at a temperature of about 650° F. (343° C.) or less in a reactor positioned in the recycle loop of the hydrocracking reactor.
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8.发明授权公开(公告)号：US11352573B2
公开(公告)日：2022-06-07
申请号：US17083439
申请日：2020-10-29
IPC分类号： C10G51/02 , C10G11/18 , B01J8/18 , B01J8/26 , C10G51/06 , B01D3/14 , B01J38/38 , C10G7/00 , C10G11/04
摘要： Methods for operating a system having two downflow high-severity FCC units for producing products from a hydrocarbon feed includes introducing the hydrocarbon feed to a feed separator and separating it into a lesser boiling point fraction and a greater boiling point fraction. The greater boiling point fraction is passed to the first FCC unit and cracked in the presence of a first catalyst at 500° C. to 700° C. to produce a first cracking reaction product and a spent first catalyst. The lesser boiling point fraction is passed to the second FCC unit and cracked in the presence of a second catalyst at 500° C. to 700° C. to produce a second cracking reaction product and a spent second catalyst. At least a portion of the spent first catalyst or the spent second catalyst is passed back to the first FCC unit, the second FCC unit or both.
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公开(公告)号：US11291927B2
公开(公告)日：2022-04-05
申请号：US17374959
申请日：2021-07-13
IPC分类号： B01D1/26 , B01D1/28 , 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： This disclosure provides systems and methods that utilize integrated mechanical vapor or thermal vapor compression to upgrade process vapors and condense them to recover the heat of condensation across multiple processes, wherein the total process energy is reduced. Existing processes that are unable to recover the heat of condensation in vapors are integrated with mechanical or thermal compressors that raise vapor pressures and temperatures sufficient to permit reuse. Integrating multiple processes permits vapor upgrading that can selectively optimize energy efficiency, environmental sustainability, process economics, or a prioritized blend of such goals. Mechanical or thermal vapor compression also alters the type of energy required in industrial processes, favoring electro-mechanical energy which can be supplied from low-carbon, renewable sources rather than combustion of carbonaceous fuels.
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公开(公告)号：US20220096955A1
公开(公告)日：2022-03-31
申请号：US17422576
申请日：2020-02-05
发明人： Selma S. Lawrence , Michael Moran , John S. Coleman , Robert S. Bartel , Vikram Singh , Monica Malhotra
摘要： Systems and methods are provided for reducing or minimizing fouling within the primary fractionator of a pyrolysis reaction system. The reduced or minimized fouling can be achieved in part by providing one or more pump-around trays in the primary fractionator below the level of the fractionation trays for an intermediate product produced by the fractionator. Including a pump-around section below the fractionation trays can improve vapor distribution within the fractionation trays, which are believed to have an increased likelihood of accumulation of foulant deposits. Optionally, other vapor distribution devices can be included along with the pump-around section.
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