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公开(公告)号：US20220119269A1
公开(公告)日：2022-04-21
申请号：US17310073
申请日：2020-01-14
Applicant: Michael Edward HUCKMAN , Scott STEVENSON , Andrew Mark WARD , Tim ABBOTT , Kenneth LAWSON , Joseph SCHROER , Zhun ZHAO , Arno OPRINS , SABIC Global Technologies B.V.
Inventor： Michael Edward HUCKMAN , Scott STEVENSON , Andrew Mark WARD , Tim ABBOTT , Kenneth Francis LAWSON , Joseph William SCHROER , Zhun ZHAO , Arno OPRINS
Abstract: An ammonia synthesis plant comprising: a feed pretreating section operable to pretreat a feed stream; a syngas generation section operable to reform the feed stream to produce a reformer product stream; a shift conversion section operable to subject the reformer product stream to the water gas shift reaction, to produce a shifted gas stream comprising more hydrogen than the reformer gas stream; a purification section operable to remove at least one component from the shifted gas stream, and provide an ammonia synthesis feed stream; and/or an ammonia synthesis section operable to produce ammonia from the ammonia synthesis feed stream, wherein the ammonia synthesis plant is configured such that, relative to a conventional ammonia synthesis plant, more of the energy required by the ammonia synthesis plant or one or more sections thereof is provided by a non-carbon based energy source, a renewable energy source, and/or electricity.
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公开(公告)号：US20220119252A1
公开(公告)日：2022-04-21
申请号：US17310077
申请日：2020-01-14
Applicant: Scott STEVENSON , Andrew Mark WARD , Kenneth Francis LAWSON , Joseph William SCHROER , Michael Edward HUCKMAN , Zhun ZHAO , SABIC Global Technologies B.V.
Inventor： Scott STEVENSON , Andrew Mark WARD , Kenneth Francis LAWSON , Joseph William SCHROER , Michael Edward HUCKMAN , Zhun ZHAO
IPC: C01B3/34 , B01J19/24 , C01B3/56 , C01B3/48 , C01C1/02 , C07C4/02 , C07C29/132 , H01M8/04082 , H01M8/0606 , B01D53/047
Abstract: A chemical synthesis plant comprising: one or more reactors configured for producing, from one or more reactants, a process stream comprising at least one chemical product; a feed preparation system configured to prepare one or more feed streams comprising one or more of the one or more reactants for introduction into the reactor; and/or a product purification system configured to separate the at least one chemical product from reaction byproducts, unreacted reactants, or a combination thereof within the process stream, wherein the chemical synthesis plant is configured such that a majority (e.g., greater than 50, 60, 70, 80, 90, or 100%) of the net energy needed for heating, cooling, compressing, or a combination thereof utilized via the one or more reactors, the feed preparation system, the product purification system, or a combination thereof is provided from an intermittent energy source (IES).
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3.发明公开公开(公告)号：US20240357713A1
公开(公告)日：2024-10-24
申请号：US18682762
申请日：2022-08-08
Applicant: SABIC GLOBAL TECHNOLOGIES B.V.
Inventor： Scott A. STEVENSON , Andrew Mark WARD , Michael Edward HUCKMAN , Hongbing JIAN , Arno Johannes Maria OPRINS , Thomas DIJKMANS , Lei CHEN , Joseph William SCHROER , Robert BROEKHUIS
CPC classification number: H05B3/66 , H05B1/0291 , H05B2203/007
Abstract: An electrically powered furnace and related methods may include an electrically powered furnace having an output of at least one megawatt with a control system; a furnace housing comprising one or more housing walls at least partially defining an interior volume; a plurality of heating zones within the interior volume; and a plurality of heated tubes extending in the interior volume. A method may include providing the feed to the electrically powered furnace; and algorithmically adjusting the output of the one or more heating elements for each of the plurality of heating zones to heat the feed to a desired temperature while maintaining temperatures of the one or more heating elements within predetermined parameters.
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4.发明申请公开(公告)号：US20180362866A1
公开(公告)日：2018-12-20
申请号：US16072428
申请日：2017-01-27
Applicant: SABIC GLOBAL TECHNOLOGIES B.V.
Inventor： Andrew Mark WARD , Arno Johannes Maria OPRINS , Egidius Jacoba Maria SCHAERLAECKENS , Raul VELASCO PELAEZ
Abstract: An integrated process to convert crude oil into petrochemical products by subjecting the crude oil to crude oil distillation to produce gases fraction, naphtha, kerosene, gasoil and resid; subjecting resid to resid upgrading to produce LPG, light-distillate and middle-distillate; subjecting at least a portion of one or more of the group consisting of middle-distillate produced by resid upgrading, kerosene and gasoil to middle-distillate hydrocracking to produce LPG, light-distillate and hydrowax; and subjecting at least a portion of one or more of the group consisting of light-distillate produced by resid upgrading, light-distillate produced by middle-distillate hydrocracking and hydrowax to steam cracking. A process installation for performing the process of the present invention is also provided, and together allow conversion of crude oil into petrochemical products having an improved carbon-efficiency, while maintaining a high ethylene yield and a favourable ethylene:propylene ratio.
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5.发明申请公开(公告)号：US20170121613A1
公开(公告)日：2017-05-04
申请号：US15120882
申请日：2014-12-23
IPC: C10G65/00
CPC classification number: C10G65/00 , C10G9/36 , C10G47/00 , C10G65/10 , C10G65/12 , C10G2400/28 , C10G2400/30
Abstract: A process for converting hydrocarbons originating from refinery operations such as atmospheric distillation unit or a fluid catalytic cracking unit (FCC), into lighter boiling hydrocracked hydrocarbons having a boiling point lower than naphthalene and lower.
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Patent Agency Ranking
公开(公告)号：US20250010264A1
公开(公告)日：2025-01-09
申请号：US18898321
申请日：2024-09-26
Applicant: SABIC Global Technologies B.V.
Inventor： Andrew Mark WARD , Scott STEVENSON , Arno OPRINS , Zhun ZHAO , Tim ABBOTT , Kenneth Francis LAWSON , Joseph William SCHROER , Michael Edward HUCKMAN
IPC: B01J19/00 , B01D53/047 , B01D53/26 , B01J4/00 , B01J6/00 , B01J19/24 , C01B3/12 , C01B3/34 , C01B3/48 , C01B3/56 , C01C1/02 , C01C1/04 , C07C4/02 , C07C4/04 , C07C29/132 , C07C29/152 , F25J3/02 , H01M8/04082 , H01M8/0606 , H01M8/0612 , H01M8/1007 , H02J15/00
Abstract: An olefin synthesis plant comprising: a feed pretreatment section configured to pretreat a feed stream; a pyrolysis section comprising one or more pyrolysis reactors configured to crack hydrocarbons in the feed stream in the presence of a diluent to produce a cracked gas stream; a primary fractionation and compression section configured to provide heat recovery from and quenching of the cracked gas stream; remove a component from the cracked gas stream; and compress the cracked gas stream, thus providing a compressed cracked gas stream; and/or a product separation section configured to separate a product olefin stream from the compressed cracked gas stream, wherein the olefin synthesis plant is configured such that, relative to a conventional olefin synthesis plant, more of the energy and/or the net energy required by the olefin synthesis plant and/or one or more sections thereof, is provided by a non-carbon based and/or renewable energy source and/or electricity.
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7.发明申请公开(公告)号：US20190039970A1
公开(公告)日：2019-02-07
申请号：US16153268
申请日：2018-10-05
Inventor： Andrew Mark WARD , Ravichander NARAYANASWAMY , Vijayanand RAJAGOPALAN , Arno Johannes Maria OPRINS , Egidius Jacoba Maria SCHAERLAECKENS , Raul VELASCO PELAEZ
IPC: C07C4/04 , C10G69/06 , C10G69/04 , C10G7/00 , C10G55/02 , C10G45/58 , C10G9/00 , C10G69/00 , C10G9/36
Abstract: The present invention relates to an integrated process to convert crude oil into petrochemical products comprising crude oil distillation, aromatic ring opening, and olefins synthesis, which process comprises subjecting a hydrocarbon feed to aromatic ring opening to produce LPG and subjecting the LPG produced in the integrated process to olefins synthesis. Furthermore, the present invention relates to a process installation to convert crude oil into petrochemical products comprising a crude distillation unit comprising an inlet for crude oil and at least one outlet for kerosene and/or gasoil; an aromatic ring opening unit comprising an inlet for a hydrocarbon feed to aromatic ring opening and an outlet for LPG; and a unit for the olefins synthesis comprising an inlet for LPG produced by the integrated petrochemical process installation and an outlet for olefins. The hydrocarbon feed subjected to aromatic ring opening comprises kerosene and/or gasoil produced by crude oil distillation in the process; and refinery unit-derived middle-distillate produced in the process. The process and the process installation of the present invention have an increased production of petrochemicals at the expense of the production of fuels and an improved propylene yield.
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公开(公告)号：US20170369795A1
公开(公告)日：2017-12-28
申请号：US15538495
申请日：2015-12-15
Applicant: SABIC Global Technologies B.V.
Inventor： Arno Johannes Maria OPRINS , Andrew P. DAVIES , Andrew Mark WARD , Kae Shin WONG , Luis ARAMBURO , Maikel van IERSEL
CPC classification number: C10G65/18 , C10G47/20 , C10G65/00 , C10G65/10 , C10G2300/1048 , C10G2400/20 , C10G2400/26 , C10G2400/28
Abstract: The invention relates to a process for producing C2 and C3 hydrocarbons, comprising a) subjecting a mixed hydrocarbon stream to first hydrocracking in the presence of a first hydrocracking catalyst to produce a first hydrocracking product stream; and b) subjecting the first hydrocarbon product stream to C4 hydrocracking optimized for converting C4 hydrocarbons into C3 hydrocarbons in the presence of a C4 hydrocracking catalyst to obtain a C4 hydrocracking product stream comprising C2 and C3 hydrocarbons.
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公开(公告)号：US20170342335A1
公开(公告)日：2017-11-30
申请号：US15538447
申请日：2015-12-15
Applicant: SABIC Global Technologies B.V.
Inventor： Arno Johannes Maria OPRINS , Andrew P. DAVIES , Andrew Mark WARD , Kae Shin WONG , Luis ARAMBURO , Maikel VAN IERSEL
CPC classification number: C10G67/02 , C10G65/00 , C10G65/10 , C10G65/18 , C10G69/02 , C10G2300/301 , C10G2400/20 , C10G2400/26 , C10G2400/28 , C10G2400/30
Abstract: The invention relates to a process for producing LPG and BTX, comprising a) subjecting a mixed hydrocarbon feedstream to first hydrocracking in the presence of a first hydrocracking catalyst to produce a first hydrocracking product stream; b) separating the first hydrocracking product stream to provide at least a light hydrocarbon stream comprising at least C2 and C3 hydrocarbons, a middle hydrocarbon stream comprising C4 and/or C5 hydrocarbons and a heavy hydrocarbon stream comprising at least C6+ hydrocarbons and c) subjecting the heavy hydrocarbon stream to second hydrocracking to produce a second hydrocracking product stream comprising BTX, wherein the second hydrocracking is more severe than the first hydrocracking, wherein at least part of the middle hydrocarbon stream is recycled back to the first hydrocracking in step a).
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公开(公告)号：US20170009151A1
公开(公告)日：2017-01-12
申请号：US15120681
申请日：2014-12-23
Applicant: Christoph DITTRICH , Joris VAN WILLIGENBURG , Egidius Jacoba Maria SCHAERLAECKENS , Andrew Mark WARD , Arno Johannes Maria OPRINS , Vijayanand RAJAGOPALAN , Ravichander NARAYANASWAMY , SAUDI BASIC INDUSTRIES CORPORATION , SABIC GLOBAL TECHNOLOGIES B.V. , Raúl VELASCO PELAEZ
Inventor： Christoph DITTRICH , Joris VAN WILLIGENBURG , Raul VELASCO PELAEZ , Egidius Jacoba Maria SCHAERLAECKENS , Andrew Mark WARD , Arno Johannes Maria OPRINS , Vijayanand RAJAGOPALAN , Ravichander NARAYANASWAMY
IPC: C10G67/00
CPC classification number: C10G67/00 , C10G69/00 , C10G69/04 , C10G69/06 , C10G2400/20 , C10G2400/30
Abstract: The present invention relates to a process for converting a hydrocarbon feedstock into olefins and preferably also into BTX, said converting process comprising the following steps of: feeding a hydrocarbon feed-stock to a first hydrocracking unit, feeding the effluent from said first hydrocracking unit to a first separation section, separating said effluent in said first separation section feeding at least one stream to a dehydrogenation unit, and feeding the effluent from said at least one dehydrogenation unit to a second separation section.
Abstract translation: 本发明涉及将烃原料转化为烯烃并优选转化成BTX的方法，所述转化方法包括以下步骤：将烃原料进料至第一加氢裂化装置，将来自所述第一加氢裂化装置的流出物送入 第一分离部分，将所述第一分离部分中的所述流出物分离，将至少一个流进料到脱氢单元，以及将来自所述至少一个脱氢单元的流出物供给到第二分离部分。
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