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公开(公告)号：US20250033017A1
公开(公告)日：2025-01-30
申请号：US18916451
申请日：2024-10-15
Applicant: SABIC Global Technologies B.V.
Inventor： Scott STEVENSON , Andrew Mark WARD , Tim ABBOTT , Kenneth Francis LAWSON , Joseph William SCHROER , Michael Edward HUCKMAN , Arno OPRINS , Zhun ZHAO
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: 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 one or more reactors; 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 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 a non-carbon based energy source, from a renewable energy source, and/or from electricity.
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公开(公告)号：US20240359154A1
公开(公告)日：2024-10-31
申请号：US18763904
申请日：2024-07-03
Applicant: SABIC Global Technologies B.V.
Inventor： Joseph William SCHROER , Scott STEVENSON , Andrew Mark WARD , Tim ABBOTT , Kenneth Francis LAWSON , Michael Edward HUCKMAN , Zhun ZHAO , Arno OPRINS
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
CPC classification number: B01J19/0053 , B01D53/047 , B01D53/265 , B01J4/008 , B01J6/008 , B01J19/0033 , B01J19/2465 , C01B3/12 , C01B3/342 , C01B3/48 , C01B3/56 , C01C1/02 , C01C1/0417 , C01C1/0488 , C07C4/02 , C07C4/04 , C07C29/132 , C07C29/152 , F25J3/0233 , H01M8/04201 , H01M8/0606 , H01M8/0618 , H02J15/006 , H02J15/008 , B01D2256/16 , B01D2256/245 , B01J2219/00051 , B01J2219/00132 , B01J2219/00761 , B01J2219/0871 , C01B2203/0216 , C01B2203/0233 , C01B2203/0238 , C01B2203/0244 , C01B2203/0261 , C01B2203/0283 , C01B2203/0294 , C01B2203/04 , C01B2203/061 , C01B2203/066 , C01B2203/068 , C01B2203/085 , C01B2203/148 , H01M8/1007
Abstract: A methanol synthesis plant comprising: a feed pretreating section operable to pretreat a feed stream; a synthesis gas (syngas) generation section comprising one or more reactors operable to produce a syngas synthesis product stream comprising synthesis gas from the feed stream; a methanol synthesis section comprising one or more methanol synthesis reactors operable to produce a synthesis product comprising methanol; and/or a methanol purification section operable to remove at least one component from the synthesis product to provide a purified methanol product; wherein the methanol synthesis plant is configured such that, relative to a conventional methanol synthesis plant, more of the net energy required by the methanol synthesis plant, the feed pretreating section, the syngas generation section, the methanol synthesis section, the methanol purification section, or a combination 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：US20220119328A1
公开(公告)日：2022-04-21
申请号：US17310074
申请日：2020-01-14
Applicant: Joseph William SCHROER , Scott STEVENSON , Andrew Mark WARD , Tim ABBOTT , Kenneth Francis LAWSON , Michael Edward HUCKMAN , Zhun ZHAO , Arno OPRINS , SABIC Global Technologies B.V.
Inventor： Joseph William SCHROER , Scott STEVENSON , Andrew Mark WARD , Tim ABBOTT , Kenneth Francis LAWSON , Michael Edward HUCKMAN , Zhun ZHAO , Arno OPRINS
IPC: C07C29/152 , C01B3/48 , H02J15/00 , H01M8/0612 , B01D53/26 , F25J3/02
Abstract: A methanol synthesis plant comprising: a feed pretreating section operable to pretreat a feed stream; a synthesis gas (syngas) generation section comprising one or more reactors operable to produce a syngas synthesis product stream comprising synthesis gas from the feed stream; a methanol synthesis section comprising one or more methanol synthesis reactors operable to produce a synthesis product comprising methanol; and/or a methanol purification section operable to remove at least one component from the synthesis product to provide a purified methanol product; wherein the methanol synthesis plant is configured such that, relative to a conventional methanol synthesis plant, more of the net energy required by the methanol synthesis plant, the feed pretreating section, the syngas generation section, the methanol synthesis section, the methanol purification section, or a combination 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：US20190352569A1
公开(公告)日：2019-11-21
申请号：US16480469
申请日：2018-02-02
Applicant: SABIC GLOBAL TECHNOLOGIES B.V.
Inventor： Arno Johannes Maria OPRINS , Andrew Mark WARD , Raul VELASCO PELAEZ , Egidius Jacoba Maria SCHAERLAECKENS , Joris VAN WILLIGENBURG
Abstract: An integrated hydrotreating and steam pyrolysis process for the direct processing of a crude oil to produce olefinic and aromatic petrochemicals by separating the crude oil into light components and heavy components.
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公开(公告)号：US20190322952A1
公开(公告)日：2019-10-24
申请号：US16404295
申请日：2019-05-06
Inventor： Andrew Mark WARD , Arno Johannes Maria OPRINS , Thomas Hubertus Maria HOUSMANS , Ravichander NARAYANASWAMY , Vijayanand RAJAGOPALAN , Lakshmikant Suryakant POWALE
Abstract: The present invention relates to process for cracking a hydrocarbon feedstock in a steam cracker unit, comprising the following steps of: feeding a hydrocarbon feedstock to a first hydrocracking unit, feeding the hydrocarbon feedstock thus cracked to a separation unit for obtaining a stream high in paraffins and naphtenes, a stream high in heavy aromatics and a stream high in mono-aromatics feeding the stream high in paraffins and naphtenes to a second hydrocracking unit, wherein the process conditions in the first hydrocracking unit differ from the process conditions in the second hydrocracking unit, separating the stream thus hydrocracked in the second hydrocracking unit in a high content aromatics stream and gaseous stream comprising C2-C4 paraffins, hydrogen and methane, feeding the gaseous stream to a steam cracker unit.
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Patent Agency Ranking
16.发明申请公开(公告)号：US20190039969A1
公开(公告)日：2019-02-07
申请号：US16153125
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：US20220127209A1
公开(公告)日：2022-04-28
申请号：US17310072
申请日：2020-01-14
Applicant: Andrew Mark WARD , Scott STEVENSON , Arno OPRINS , Zhun ZHAO , Tim ABBOTT , Kenneth Francis LAWSON , Joseph William SCHROER , Michael Edward HUCKMAN , 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: C07C4/04 , B01J6/00 , H02J15/00 , H01M8/1007
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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公开(公告)号：US20220126251A1
公开(公告)日：2022-04-28
申请号：US17310076
申请日：2020-01-14
Applicant: SABIC Global Technologies B.V.
Inventor： Scott STEVENSON , Andrew Mark WARD , Tim ABBOTT , Kenneth Francis LAWSON , Joseph William SCHROER , Michael Edward HUCKMAN , Arno OPRINS , Zhun ZHAO
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 one or more reactors; 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 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 a noncarbon based energy source, from a renewable energy source, and/or from electricity.
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公开(公告)号：US20200017779A1
公开(公告)日：2020-01-16
申请号：US16584096
申请日：2019-09-26
Abstract: The present invention relates to a process for cracking a hydrocarbon feedstock in a steam cracker unit, comprising the following steps of: feeding a liquid hydrocarbon feedstock to a hydrocracking unit, separating the stream thus hydrocracked in said hydrocracking unit into a high content aromatics stream and a gaseous stream comprising C2-C4 paraffins, hydrogen and methane, separating C2-C4 paraffins from said gaseous stream, feeding said C2-C4 paraffins thus separated to the furnace section of a steam cracker unit.
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公开(公告)号：US20190390124A1
公开(公告)日：2019-12-26
申请号：US16481756
申请日：2018-02-02
Applicant: SABIC GLOBAL TECHNOLOGIES B.V.
Inventor： Arno Johannes Maria OPRINS , Andrew Mark WARD , Egidius Jacoba Maria SCHAERLAECKENS , Joris VAN WILLIGENBURG
IPC: C10G69/06
Abstract: Integrated hydrotreating and steam pyrolysis processes for the direct processing of a crude oil to produce olefinic and aromatic petrochemicals.
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