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1.发明申请
公开(公告)号：WO2021163236A1
公开(公告)日：2021-08-19
申请号：PCT/US2021/017524
申请日：2021-02-11
摘要： The present application provides systems and methods for producing isononanol and gasoline and diesel blending components. In at least one embodiment of the present systems and methods, a hydrocarbon feed is cracked in a steam cracker to form a first ethylene stream, a first propylene stream, and a C4 stream comprising isobutene and butadiene. The C4 stream is reacted with a methanol stream in a methyl tertiary butyl ether (MTBE) unit to form MTBE and a butadiene-rich C4 stream. The butadiene-rich C4 stream is selectively hydrogenated in a butadiene unit to form a butene-rich C4 stream. The butene-rich C4 stream undergoes a series of reactions in an isononanol unit to produce isononanol and an olefin-rich stream. The olefin-rich stream is then separate, in a separation unit, a C8, C12, and C16 fuel oil streams.
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公开(公告)号：WO2021113249A1
公开(公告)日：2021-06-10
申请号：PCT/US2020/062723
申请日：2020-12-01
IPC分类号： C10G21/00 , C10G45/00 , C10G47/00 , C10G9/36 , C01B3/34 , B01D53/047 , C01B3/12 , C01B3/48 , C10G2/00 , C10K3/04 , C10G55/02 , C10G67/04 , C10G69/02 , C10G57/00 , F02C1/00 , C10G9/00
摘要： A processing facility is provided. The processing facility includes an asphaltenes and metals (AM) removal system configured to process a feed stream to produce a power generation stream, a hydroprocessing feed stream, and an asphaltenes stream. A power generation system is fed by the power generation feed stream. A hydroprocessing system is configured to process the hydroprocessing feed stream to form a gas stream and a liquid stream. A hydrogen production system is configured to produce hydrogen, carbon monoxide and carbon dioxide from the gas feed stream. A carbon dioxide conversion system is configured to produce synthetic hydrocarbons from the carbon dioxide, and a cracking system is configured to process the liquid feed stream.
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3.发明申请
公开(公告)号：WO2021101557A1
公开(公告)日：2021-05-27
申请号：PCT/US2019/062732
申请日：2019-11-22
发明人： ZHANG, Shuguang
IPC分类号： C10G45/00 , C10G47/00 , C10G65/14 , C10G1/00 , C10G7/08 , C10G35/00 , C10G69/08 , C07C7/14 , C07C7/144 , C10G21/00
摘要： Processes for separating the components in coal derived liquids are described. The coal derived liquid is first separated into polar compounds and non-polar compounds. The polar and non-polar compounds are further separated. Appropriate conditions are then applied to process the various compounds in order to maximize the yield of chemicals (phenols, aromatics) and/or transportation fuels (gasoline, diesel, etc.), and catalyst life while minimizing the consumption of hydrogen, lowering the severity of reaction conditions, and simplifying operations.
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4.发明申请
公开(公告)号：WO2021071894A1
公开(公告)日：2021-04-15
申请号：PCT/US2020/054506
申请日：2020-10-07
发明人： KOSEOGLU, Omer, Refa
摘要： A process for the economical and environmentally acceptable disposal of spent adsorbent recovered from an adsorption column used to remove HPNA compounds and HPNA precursors from hydrocracking unit bottoms and/or recycle streams includes removing the liquid hydrocarbon oil from the spent adsorbent material by a combination of solvent flushing, and/or heating and vacuum treatment, grinding the dried adsorbent material containing the HPNA compounds and HPNA precursors to produce free-flowing particles of a predetermined maximum size, and introducing the particulate adsorbent material into a membrane wall partial oxidation gasification reactor to produce hydrogen and carbon monoxide synthesis gas, or syngas, which can be further processed by the water-gas shift reaction to increase the overall hydrogen recovered from the initial feed to the gasifier.
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公开(公告)号：WO2021045885A1
公开(公告)日：2021-03-11
申请号：PCT/US2020/046278
申请日：2020-08-14
摘要： An hydroconverted effluent composition is provided, along with systems and methods for making such a composition. The hydroconverted effluent composition can have 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 hydroconverted effluent 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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6.发明申请
公开(公告)号：WO2021008924A1
公开(公告)日：2021-01-21
申请号：PCT/EP2020/069036
申请日：2020-07-06
IPC分类号： C10G9/36 , C10G47/00 , C10G65/12 , C10G45/02 , C10G67/04 , C10G69/06 , C10G21/00 , C10G21/14
摘要： La présente invention concerne un procédé de production d'oléfines à partir d'une charge 11 hydrocarbonée ayant une teneur en soufre d'au moins 0,1 % poids, une température initiale d'ébullition d'au moins 180°C et une température finale d'ébullition d'au moins 600°C.
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公开(公告)号：WO2020178597A1
公开(公告)日：2020-09-10
申请号：PCT/GB2020/050534
申请日：2020-03-06
摘要： A process for upgrading a pyrolysis oil comprising treating a pyrolysis oil with an aqueous solution and optionally a hydrocarbon fluid, wherein the pyrolysis oil is a derived from the pyrolysis of plastic or rubber, or a combination thereof;and an upgraded pyrolysis oil prepared by said process.
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8.发明申请
公开(公告)号：WO2020086251A1
公开(公告)日：2020-04-30
申请号：PCT/US2019/054956
申请日：2019-10-07
发明人： KOSEOGLU, Omer, Refa
摘要： The invention is an integrated process for treating residual oil of a hydrocarbon feedstock. The oil is first subjected to solvent deasphalting then gas phase oxidative desulfurization. Additional, optional steps including hydrodesulfurization, and hydrocracking, may also be incorporated in t o the integrated process.
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公开(公告)号：WO2018122274A1
公开(公告)日：2018-07-05
申请号：PCT/EP2017/084668
申请日：2017-12-27
发明人： BRU, Ariel , VAN DIJK, Nicolaas , VAN HASSELT, Bastiaan, Willem , BINNEVELD, Eduardus, Theodorus, Cornelis , MEIJER, Eduard , STICHTER, Hendrik
摘要： The invention provides a process for producing middle distillates from a residual hydrocarbonaceous feedstock, comprising the steps of: (a) thermally cracking the residual hydrocarbonaceous feedstock in a first thermal cracking unit to obtain a thermally cracked product comprising a thermally cracked residue; (b) deasphalting at least the thermally cracked residue to obtain a thermally cracked deasphalted oil and an asphaltic product; (c) thermally cracking at least part of the thermally cracked deasphalted oil in a second thermal cracking unit to obtain a twice thermally cracked deasphalted oil; (d) hydrocracking at least part of the twice thermally cracked deasphalted oil as obtained in step (c) to obtain a hydrocracked product; and (e) subjecting at least part of the hydrocracked product as obtained in step (d) to a separation treatment to obtain at least a middle distillate fraction. The invention further provides a process for producing ultra-low sulphur fuel oil and middle distillates and a low-sulphur fuel oil or fuel oil blending component having a sulphur content in the range of from 0.03%wt. to less than 0.5%wt.
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