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21.
公开(公告)号:AU2020289191A1
公开(公告)日:2021-12-23
申请号:AU2020289191
申请日:2020-05-28
Applicant: BASF SE , THYSSENKRUPP AG , THYSSENKRUPP IND SOLUTIONS AG
Inventor: SCHEIFF FREDERIK , LEDUC MARC , BODE ANDREAS , BUEKER KARSTEN , ANTWEILER NICOLAI
Abstract: The invention relates to a method for treating an exhaust gas flow (9) arising in a system (7) for producing aluminium via the electrolytic reduction of aluminium oxide in a melt, using at least one anode made of a carbon-containing material, said exhaust gas flow containing carbon oxides due to the reduction of the aluminium oxide by means of the carbon, wherein, according to the invention, at least one sub-flow of the carbon oxide contained in the exhaust gas flow is reacted with hydrogen (23) or mixed with a hydrogen flow and then supplied for utilisation. After a purification and conditioning of the exhaust gas flow in a device (16), e.g. an enrichment with carbon monoxide can then be carried out in a reactor (20) and the syngas obtained in this way can be supplied to a chemical or biotechnological system (25) for the synthesis of valuable chemical substances.
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22.
公开(公告)号:CA3142546A1
公开(公告)日:2020-12-10
申请号:CA3142546
申请日:2020-05-28
Applicant: BASF SE , THYSSENKRUPP AG , THYSSENKRUPP IND SOLUTIONS AG
Inventor: SCHEIFF FREDERIK , LEDUC MARC , KOLIOS GRIGORIOS , DALOZ WILLIAM , BUEKER KARSTEN , ANTWEILER NICOLAI , BODE ANDREAS
Abstract: The present invention relates to an integrated process containing the following steps (i) pyrolysis of hydrocarbons to carbon and hydrogen, (iia) removal of at least a part of the produced carbon in step (i) and at least partly further processing of said carbon into a carbon containing electrode, (iib) removal of the hydrogen produced in step (i) and at least partly use said hydrogen for providing energy, preferably electric energy or heat, for the electrode production in step (iia). In addition, the present invention relates to a joint plant containing (a) at least one reactor for pyrolysis process, (b) at least one reactor for the production of electrodes for an aluminum process, (c) a power plant and/or at least one gas-fired burner and optionally (d) at least one reactor for the electrolysis for producing aluminum.
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公开(公告)号:ZA201400783B
公开(公告)日:2017-11-29
申请号:ZA201400783
申请日:2014-02-03
Inventor: SCHNEIDER CHRISTIAN , MACHHAMMER OTTO , MAASS HANS-JUERGEN , KOLIOS GRIGORIOS , KLINGLER DIRK , KERN MATTHIAS , HORMUTH WOLFGANG ALOIS , GUZMANN MARCUS , GOEKE VOLKER , BODE ANDREAS
Abstract: The invention relates to a process for parallel preparation of hydrogen and one or more carbonaceous products, in which hydrocarbons are introduced into a reaction space (R) and decomposed thermally to carbon and hydrogen in the presence of carbon-rich pellets (W). It is a feature of the invention that at least a portion of the thermal energy required for the hydrocarbon decomposition is introduced into the reaction space (R) by means of a gaseous heat carrier.
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公开(公告)号:AU2013357293A1
公开(公告)日:2015-07-23
申请号:AU2013357293
申请日:2013-12-12
Inventor: MACHHAMMER OTTO , HORMUTH WOLFGANG ALOIS , SCHNEIDER CHRISTIAN , BODE ANDREAS , GOEKE VOLKER , MAASS HANS-JUERGEN , KERN MATTHIAS , KLINGLER DIRK , KONIG RENE , BRUGGEMANN PHILIPP , BERNNAT JENS , KOLIOS GRIGORIOS
Abstract: The invention relates to a method for performing endothermic process, characterized in that the annual average total energy required for the endothermic process originates from at least two different energy sources. One of the energy sources is an electrical energy source, the power of which varies between 0 and 100% of the required total power, and three different energy modes individually can provide the total required power for the endothermic process: (i) exclusively electrical energy, (ii) a mixture of electrical energy and at least one additional non-energy source, or (iii) exclusively non-electrical energy. The transition time in which the change from one energy mode to another energy mode is completed 30 minutes at most.
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公开(公告)号:AU2012280624A1
公开(公告)日:2014-02-20
申请号:AU2012280624
申请日:2012-07-05
Inventor: MASS HANS-JURGEN , GOKE VOLKER , MACHHAMMER OTTO , GUZMANN MARCUS , SCHNEIDER CHRISTIAN , HORMUTH WOLFGANG ALOIS , BODE ANDREAS , KLINGLER DIRK , KERN MATTHIAS , KOLIOS GRIGORIOS
Abstract: Process for the production of synthesis gas (3), in which methane and carbon dioxide (2) are introduced into a reaction space (R) and reacted in the presence of a solid (W) at elevated temperatures to give hydrogen and carbon monoxide. Methane and carbon dioxide are passed through a carbon-containing granular material (W) and reacted in a high-temperature zone (H).
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公开(公告)号:AU2008240334A1
公开(公告)日:2009-05-21
申请号:AU2008240334
申请日:2008-10-31
Applicant: BASF SE
Inventor: BECHTOFF BERND , WUNSCH JOSEF RICHARD , KAROS MARVIN , BAUS ULF , GUZMANN MARCUS , HUFF JRGEN , SCHOLTISSEK MARTIN , BODE ANDREAS , BOLLSCHWELLER CLAUS
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公开(公告)号:ES2991383T3
公开(公告)日:2024-12-03
申请号:ES20716701
申请日:2020-03-31
Applicant: BASF SE , THYSSENKRUPP UHDE GMBH , THYSSENKRUPP AG
Inventor: ZANDER HANS-JÖRG , WEIKL MARKUS , BODE ANDREAS , KLINGLER DIRK , KERN MATTHIAS , KOLIOS GRIGORIOS , WECHSUNG ACHIM , SCHEIFF FREDERIK , FLICK DIETER , ANTWEILER NICOLAI , BÜKER KARSTEN
Abstract: La invención se refiere a un reactor (1) para llevar a cabo una reacción endotérmica, en particular una reacción a alta temperatura, en la que se obtiene un gas producto (P) a partir de un gas de alimentación (E), en el que: el reactor (1) rodea un interior de reactor (10); el reactor (1) está configurado para proporcionar un lecho de reactor (120) en una zona de reacción (12) del interior de reactor (10), lecho de reactor que comprende un gran número de partículas de material sólido (F); el reactor (1) también está configurado para guiar el gas de alimentación (E) hacia la zona de reacción (12); para calentar el gas de alimentación (E), el reactor (1) está diseñado para calentar las partículas de material sólido (F) en la zona de reacción (12) de tal manera que, mediante la transferencia de calor desde las partículas de material sólido (F) al gas de alimentación (E), el gas de alimentación (E) en la zona de reacción (12) puede calentarse a una temperatura de reacción para participar como un producto de partida en la reacción endotérmica para producir el gas producto (P); y el interior del reactor (10) comprende además una primera zona de integración térmica (11) en la que el calor del gas producto (P) producido en la zona de reacción (12) puede transferirse a partículas de material sólido (F) del lecho del reactor (120) que deben ser conducidas a la zona de reacción (12); y el interior del reactor (10) comprende además una segunda zona de integración térmica (13) en la que el calor de las partículas de material sólido (F) del lecho del reactor (12) procedentes de la zona de reacción (12) puede transferirse al gas de alimentación (E) para precalentar el gas de alimentación (E). La invención también se refiere a un procedimiento en el que se utiliza un reactor (1) según la invención. (Traducción automática con Google Translate, sin valor legal)
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公开(公告)号:CA2839717C
公开(公告)日:2022-03-29
申请号:CA2839717
申请日:2012-07-05
Inventor: MASS HANS-JURGEN , GOKE VOLKER , MACHHAMMER OTTO , GUZMANN MARCUS , SCHNEIDER CHRISTIAN , HORMUTH WOLFGANG ALOIS , BODE ANDREAS , KLINGLER DIRK , KERN MATTHIAS , KOLIOS GRIGORIOS
Abstract: Process for the production of synthesis gas (3), in which methane and carbon dioxide (2) are introduced into a reaction space (R) and reacted in the presence of a solid (W) at elevated temperatures to give hydrogen and carbon monoxide. Methane and carbon dioxide are passed through a carbon-containing granular material (W) and reacted in a high-temperature zone (H).
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公开(公告)号:DE102019002523A8
公开(公告)日:2022-02-24
申请号:DE102019002523
申请日:2019-04-05
Applicant: BASF SE , LINDE GMBH , THYSSENKRUPP AG , THYSSENKRUPP IND SOLUTIONS AG
Inventor: BODE ANDREAS , FLICK DIETER , KERN MATTHIAS , KLINGLER DIRK , SCHEIFF FREDERIK , WECHSUNG ACHIM , WEIKL MARKUS , ZANDER HANS-JÖRG , KOLIOS GRIGORIOS , ANTWEILER NICOLAI , BÜKER KARSTEN DR
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公开(公告)号:AU2020250684A1
公开(公告)日:2021-10-28
申请号:AU2020250684
申请日:2020-03-31
Applicant: BASF SE , THYSSENKRUPP AG , THYSSENKRUPP IND SOLUTIONS AG
Inventor: ZANDER HANS-JÖRG , WEIKL MARKUS , BODE ANDREAS , KLINGLER DIRK , KERN MATTHIAS , KOLIOS GRIGORIOS , WECHSUNG ACHIM , SCHEIFF FREDERIK , FLICK DIETER , ANTWEILER NICOLAI , BÜKER KARSTEN
Abstract: The invention relates to a reactor (1) for carrying out an endothermic reaction, in particular a high-temperature reaction, in which a product gas (P) is obtained from a feed gas (E), wherein: the reactor (1) surrounds a reactor interior (10); the reactor (1) is configured to provide a reactor bed (120) in a reaction zone (12) of the reactor interior (10), which reactor bed comprises a large number of solid material particles (F); the reactor (1) is also configured to guide the feed gas (E) into the reaction zone (12); in order to heat the feed gas (E), the reactor (1) is designed to heat the solid material particles (F) in the reaction zone (12) such that, by transferring heat from the solid material particles (F) to the feed gas (E), the feed gas (E) in the reaction zone (12) can be heated to a reaction temperature in order to participate as a starting product in the endothermic reaction for producing the product gas (P); and the reactor interior (10) also comprises a first heat integration zone (11) in which heat from the product gas (P) produced in the reaction zone (12) can be transferred to solid material particles (F) of the reactor bed (120) which are to be guided into the reaction zone (12); and the reactor interior (10) also comprises a second heat integration zone (13) in which heat from solid material particles (F) of the reactor bed (12) coming from the reaction zone (12) can be transferred to the feed gas (E) in order to preheat the feed gas (E). The invention also relates to a method in which a reactor (1) according to the invention is used.
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