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1.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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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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公开(公告)号：US20240299901A1
公开(公告)日：2024-09-12
申请号：US18574584
申请日：2022-06-27
Applicant: SABIC GLOBAL TECHNOLOGIES B.V.
Inventor： Arno Johannes Maria OPRINS , Michael Edward HUCKMAN , Joseph William SCHROER , Balamurali Krishna NAIR
CPC classification number: B01J19/0013 , B01D1/0017 , B01J19/245 , B01J2219/00092 , B01J2219/00128
Abstract: A system and method for cracking hydrocarbon feed streams may include a pre-heating assembly configured to heat the hydrocarbon feed stream to provide a pre-heated feed stream including a vaporized portion and a pre-heated liquid portion. The pre-heating assembly may include an electrically-powered heater, an electrically-powered heater and a steam heater, or an electrically-powered heater and heat transfer fluid configured to heat the feed stream. The pre-heating assembly also may include a flash device positioned to receive the vaporized portion and the pre-heated liquid portion and separate the vaporized portion of the pre-heated feed stream or the pre-heated liquid hydrocarbon feed stream from the remaining liquid portion of the feed stream to supply a flash device outlet stream. The system further may include a steam cracking furnace positioned to receive the flash device outlet stream and heat the flash outlet device stream to provide a product stream including cracked hydrocarbons.
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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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Patent Agency Ranking
公开(公告)号：US20220135497A1
公开(公告)日：2022-05-05
申请号：US17310228
申请日：2019-01-31
Applicant: SABIC Global Technologies B.V.
Inventor： Travis CONANT , Dustin FICKEL , Raul VELASCO PELAEZ , Joseph William SCHROER
Abstract: Disclosed are systems and processes to produce aromatic and olefinic compounds by aromatization and thermal cracking of hydrocarbons.
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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：US20250129297A1
公开(公告)日：2025-04-24
申请号：US18685459
申请日：2022-08-22
Applicant: SABIC GLOBAL TECHNOLOGIES B.V. , ARVOS GmbH
Inventor： Raul VELASCO PELAEZ , Scott A. STEVENSON , Michael Edward HUCKMAN , Arno Johannes Maria OPRINS , Joseph William SCHROER , Jens HETZER , Jörg WEIDENFELLER , Michael OLBRICHT , Andreas LINNENKOHL , Thorsten SCHLIETER
Abstract: A method to produce olefins may include supplying a hydrocarbon feed to an outer tube of a thermal energy recovery assembly; heating the hydrocarbon feed in the outer tube of the thermal energy recovery assembly to output a preheated hydrocarbon feed; supplying the preheated hydrocarbon feed to an electrically powered cracking furnace comprising a reaction zone to heat the preheated hydrocarbon feed; cracking the preheated hydrocarbon feed in the reaction zone of the electrically heated cracking furnace using heat generated by electricity to output hot reactor effluent comprising cracked hydrocarbons and olefins; supplying the hot reactor effluent to an inner tube of the thermal energy recovery assembly; and cooling the hot reactor effluent in the inner tube of the thermal energy recovery assembly by transferring heat to the hydrocarbon feed.
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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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