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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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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.发明公开公开(公告)号：US20240353179A1
公开(公告)日：2024-10-24
申请号：US18682781
申请日：2022-08-08
Applicant: SABIC GLOBAL TECHNOLOGIES B.V.
Inventor： Scott A. STEVENSON , Michael Edward HUCKMAN , Hongbing JIAN
CPC classification number: F27D99/0006 , F27D1/0036 , F27D11/02
Abstract: An electrically powered furnace may include a furnace housing and heating elements extending in the furnace housing. The furnace also may include heating tubes extending in the interior volume, and each of the heating tubes may define an interior passage positioned to receive and heat the feed as the feed passes through the interior passage. The heating tubes may be positioned in the furnace housing to receive heat radiated from the heating elements, and the heating tubes may be arranged in one or more of at least two rows or at least two columns and such that each of the heating tubes is substantially equidistant from three or more of the heating elements. A method may include supplying a feed to the heating tubes, heating the heating tubes via the heating elements, and heating the feed via as the feed passes through the heating tubes.
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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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Patent Agency Ranking
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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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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