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1.发明申请METHOD FOR THE PARALLEL PRODUCTION OF HYDROGEN AND CARBON-CONTAINING PRODUCTS 审中-公开工艺制备氢气和含碳产品的平行生产
公开(公告)号：WO2013004398A2
公开(公告)日：2013-01-10
申请号：PCT/EP2012002877
申请日：2012-07-05
Applicant: LINDE AG , MAAS HANS-JUERGEN , GOEKE VOLKER , MACHHAMMER OTTO , GUZMANN MARCUS , SCHNEIDER CHRISTIAN , HORMUTH WOLFGANG , BODE ANDREAS , KLINGLER DIRK , KERN MATTHIAS , KOLIOS GRIGORIOS , BASF SE
Inventor： MAAS HANS-JUERGEN , GOEKE VOLKER , MACHHAMMER OTTO , GUZMANN MARCUS , SCHNEIDER CHRISTIAN , HORMUTH WOLFGANG , BODE ANDREAS , KLINGLER DIRK , KERN MATTHIAS , KOLIOS GRIGORIOS
CPC classification number: C01B3/24 , C01B3/28 , C01B3/30 , C01B32/05 , C01B2203/0272 , C01B2203/04 , C01B2203/0425 , C01B2203/0485 , C01B2203/049 , C01B2203/06 , C01B2203/0805 , C01B2203/0811 , C01B2203/0822 , C01B2203/0827 , C01B2203/0866 , C01B2203/1235 , C01B2203/1258 , C10B57/005 , Y02P20/128
Abstract: The invention relates to a method for the parallel production of hydrogen and of one or more carbon-containing products. In the method, hydrocarbons are introduced into a reaction chamber (R) and are thermally decomposed into carbon and hydrogen in the presence of a carbon-rich granulated material (W). The invention is characterised in that at least a portion of the thermal energy necessary for the decomposition of the hydrocarbon is introduced into the reaction chamber (R) via a gaseous heat transfer medium.
Abstract translation: 本发明涉及一种用于同时生产氢和一种或多种含碳产品，其中，在一个反应空间（R）烃被引入的，并在富碳颗粒（W）的存在下热分解成碳和氢。 本发明是通过一种气态传热介质到反应空间（R）被引入，其特征在于在所要求的用于烃的热能的分解的至少一个部分。
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2.发明申请METHOD FOR THE PARALLEL PRODUCTION OF HYDROGEN AND CARBON-CONTAINING PRODUCTS 审中-公开工艺制备氢气和含碳产品的平行生产
公开(公告)号：WO2013004398A3
公开(公告)日：2013-04-11
申请号：PCT/EP2012002877
申请日：2012-07-05
Applicant: LINDE AG , MAABETA HANS-JUERGEN , GOEKE VOLKER , MACHHAMMER OTTO , GUZMANN MARCUS , SCHNEIDER CHRISTIAN , HORMUTH WOLFGANG , BODE ANDREAS , KLINGLER DIRK , KERN MATTHIAS , KOLIOS GRIGORIOS , BASF SE
Inventor： MAABETA HANS-JUERGEN , GOEKE VOLKER , MACHHAMMER OTTO , GUZMANN MARCUS , SCHNEIDER CHRISTIAN , HORMUTH WOLFGANG , BODE ANDREAS , KLINGLER DIRK , KERN MATTHIAS , KOLIOS GRIGORIOS
CPC classification number: C01B3/24 , C01B3/28 , C01B3/30 , C01B32/05 , C01B2203/0272 , C01B2203/04 , C01B2203/0425 , C01B2203/0485 , C01B2203/049 , C01B2203/06 , C01B2203/0805 , C01B2203/0811 , C01B2203/0822 , C01B2203/0827 , C01B2203/0866 , C01B2203/1235 , C01B2203/1258 , C10B57/005 , Y02P20/128
Abstract: The invention relates to a method for the parallel production of hydrogen (3) and of one or a plurality of carbon-containing products (8). In the method, hydrocarbons (2) are introduced into a reaction chamber (R) and are thermally decomposed into carbon and hydrogen in the presence of a carbon-rich granulated material (W). The invention is characterised in that at least a portion of the thermal energy necessary for the decomposition of the hydrocarbons is introduced into the reaction chamber (R) via a gaseous heat transfer medium.
Abstract translation: 一种用于同时生产氢气和含碳的产物的本发明的方法涉及一种方法，用于同时产生氢气的（3）和一个或更多个含碳产品富碳（8），其中，所述烃在反应空间（R）被引入，并在存在（2） 颗粒（W）被热分解成碳和氢。 本发明是通过一种气态传热介质到反应空间（R）被引入，其特征在于在所要求的用于烃的热能的分解的至少一个部分。
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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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Patent Agency Ranking
公开(公告)号：DE102015015968A1
公开(公告)日：2017-06-01
申请号：DE102015015968
申请日：2015-12-01
Applicant: BASF SE , LINDE AG , THYSSENKRUPP AG , THYSSENKRUPP IND SOLUTIONS AG
Inventor： MAASS HANS-JÜRGEN , BÜKER KARSTEN , GÖKE VOLKER , KOLIOS GRIGORIOS , BODE ANDREAS , MACHHAMMER OTTO
Abstract: Die Erfindung betrifft ein Verfahren zur Erzeugung von Synthesegas (5), bei dem kohlenwasserstoffhaltiges Koksgas (2) in einer ersten Reaktionszone (Z1) thermisch in Wasserstoff und Kohlenstoff zersetzt und dabei entstehender Wasserstoff aus der ersten Reaktionszone (Z1) in eine zweite Reaktionszone (Z2) geleitet wird, um dort mit kohlendioxidhaltigem Konvertergas (4) durch eine Reverse Wassergas-Shift Reaktion zu Wasser und Kohlenmonoxid umgesetzt zu werden, wobei, die für die thermische Zersetzung des kohlenwasserstoffhaltigen Koksgases (2) benötigte Energie der ersten Reaktionszone (Z1) aus der zweiten Reaktionszone (Z2) zugeführt wird.
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公开(公告)号：DE102015015531A1
公开(公告)日：2017-06-01
申请号：DE102015015531
申请日：2015-12-01
Applicant: BASF SE , LINDE AG , THYSSENKRUPP AG , THYSSENKRUPP IND SOLUTIONS AG
Inventor： MAASS HANS-JÜRGEN , BÜKER KARSTEN , GÖKE VOLKER , KOLIOS GRIGORIOS , BODE ANDREAS , MACHHAMMER OTTO
Abstract: Verfahren zur Erzeugung von Synthesegas (5) beim dem ein kohlenwasserstoffhaltiges Koksgas (2) und ein kohlendioxidhaltiges Konvertergas (4) in eine erste Reaktionszone (Z1) eingeleitet werden und Wasserstoff, enthalten im kohlenwasserstoffhaltigen Koksgas (2), zumindest teilweise mit Kohlendioxid zu Wasser und das Wasser mit dem Kohlenwasserstoff thermisch zu Synthesegas, welches Kohlenmonoxid und Wasserstoff enthält, umgesetzt werden. Sowie dass in einer zweiten Reaktionszone (Z2) ein sauerstoffhaltiges Gas (3) eingeleitet wird und mit diesem und einem Teil des Wasserstoff aus der ersten Reaktionszone (Z1) thermische Energie erzeugt wird, wobei, die die in der zweiten Reaktionszone (Z2) erzeugte thermische Energie der ersten Reaktionszone (Z1) zugeführt wird.
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公开(公告)号：ES2552528T3
公开(公告)日：2015-11-30
申请号：ES12734811
申请日：2012-07-05
Inventor： MASS HANS-JÜRGEN , GÖKE VOLKER , MACHHAMMER OTTO , GUZMANN MARCUS , SCHNEIDER CHRISTIAN , HORMUTH WOLFGANG ALOIS , BODE ANDREAS , KLINGLER DIRK , KERN MATTHIAS , KOLIOS GRIGORIOS
Abstract: Procedimiento para la generación de gas de síntesis, en el que se introducen metano y dióxido de carbono en un recinto de reacción y se hacen reaccionar en un lecho sólido con contenido en carbono para dar hidrógeno y monóxido de carbono, caracterizado por que el lecho sólido con contenido en carbono es conducido como lecho móvil a través del recinto de reacción, en donde el gas de síntesis formado en el recinto de reacción es conducido en contracorriente al lecho móvil y en este caso es enfriado en intercambio de calor directo con el sólido con contenido en carbono.
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公开(公告)号：AU2012280631A2
公开(公告)日：2014-05-08
申请号：AU2012280631
申请日：2012-07-05
Inventor： MAASS HANS-JURGEN , GOKE VOLKER , MACHHAMMER OTTO , GUZMANN MARCUS , SCHNEIDER CHRISTIAN , HORMUTH WOLFGANG , BODE ANDREAS , KLINGLER DIRK , KERN MATTHIAS , KOLIOS GRIGORIOS
Abstract: The invention relates to a method for the parallel production of hydrogen (3) and of one or a plurality of carbon-containing products (8). In the method, hydrocarbons (2) are introduced into a reaction chamber (R) and are thermally decomposed into carbon and hydrogen in the presence of a carbon-rich granulated material (W). The invention is characterised in that at least a portion of the thermal energy necessary for the decomposition of the hydrocarbons is introduced into the reaction chamber (R) via a gaseous heat transfer medium.
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公开(公告)号：CA2894958C
公开(公告)日：2021-04-06
申请号：CA2894958
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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