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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：CA2965415A1
公开(公告)日：2016-04-28
申请号：CA2965415
申请日：2015-10-23
Applicant: BASF SE
Inventor： KONIG RENE , KOBAN WIELAND , MILANOV ANDRIAN , SCHWAB EKKEHARD , SCHUNK STEPHAN A , LIZANDARA CARLOS , WASSERSCHAFF GUIDO
Abstract: The invention relates to a method for producing aluminates of general formula (I): A1BxAl12-xO19-y, wherein A means at least one element from the group consisting of Sr, Ba, and La, B means at least one element from the group consisting of Mn, Fe Co, Ni, Rh, Cu, and Zn, x means 0.05 to 1.0, and y means a value that is determined by the oxidation states of the other elements, comprising the following steps: (i) providing one or more solutions or suspensions containing precursor compounds of elements A and B and a precursor compound of aluminum in a solvent, (ii) converting the solutions or suspensions or the suspensions into an aerosol, (iii) introducing the aerosol into a directly or indirectly heated pyrolysis zone, (iv) performing the pyrolysis, and (v) separating the formed particles containing hexaaluminate of general formula (I) from the pyrolysis gas.
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公开(公告)号：AU2013365822A1
公开(公告)日：2015-07-23
申请号：AU2013365822
申请日：2013-12-17
Applicant: BASF SE
Inventor： KERN MATTHIAS , GLENK FRIEDRICH , KLINGLER DIRK , BODE ANDREAS , KOLIOS GRIGORIOS , SCHUNK STEPHAN , WASSERSCHAFF GUIDO , BERNNAT JENS , ZOELS BERND , SCHMIDT SABINE , KONIG RENE
Abstract: The invention relates to a process for the parallel preparation of hydrogen, carbon monoxide and a carbon-comprising product, wherein one or more hydrocarbons are thermally decomposed and at least part of the pyrolysis gas formed is taken off from the reaction zone of the decomposition reactor at a temperature of from 800 to 1400°C and reacted with carbon dioxide to form a gas mixture comprising carbon monoxide and hydrogen (synthesis gas).
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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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Patent Agency Ranking
公开(公告)号：CA2895924A1
公开(公告)日：2014-06-26
申请号：CA2895924
申请日：2013-12-17
Applicant: BASF SE
Inventor： KERN MATTHIAS , GLENK FRIEDRICH , KLINGLER DIRK , BODE ANDREAS , KOLIOS GRIGORIOS , SCHUNK STEPHAN , WASSERSCHAFF GUIDO , BERNNAT JENS , ZOELS BERND , SCHMIDT SABINE , KONIG RENE
Abstract: The invention relates to a process for the parallel preparation of hydrogen, carbon monoxide and a carbon-comprising product, wherein one or more hydrocarbons are thermally decomposed and at least part of the pyrolysis gas formed is taken off from the reaction zone of the decomposition reactor at a temperature of from 800 to 1400°C and reacted with carbon dioxide to form a gas mixture comprising carbon monoxide and hydrogen (synthesis gas).
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公开(公告)号：CA2895924C
公开(公告)日：2021-03-16
申请号：CA2895924
申请日：2013-12-17
Applicant: BASF SE
Inventor： KERN MATTHIAS , GLENK FRIEDRICH , KLINGLER DIRK , BODE ANDREAS , KOLIOS GRIGORIOS , SCHUNK STEPHAN , WASSERSCHAFF GUIDO , BERNNAT JENS , ZOELS BERND , SCHMIDT SABINE , KONIG RENE
Abstract: The invention relates to a process for the parallel preparation of hydrogen, carbon monoxide and a carbon-comprising product, wherein one or more hydrocarbons are thermally decomposed and at least part of the pyrolysis gas formed is taken off from the reaction zone of the decomposition reactor at a temperature of from 800 to 1400°C and reacted with carbon dioxide to form a gas mixture comprising carbon monoxide and hydrogen (synthesis gas).
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公开(公告)号：UA115346C2
公开(公告)日：2017-10-25
申请号：UAA201507131
申请日：2013-12-13
Applicant: BASF SE , LINDE AG , THYSSENKRUPP IND SOLUTIONS AG
Inventor： SCHNEIDER CHRISTIAN , BODE ANDREAS , KLINGLER DIRK , MACHHAMMER OTTO , BRUGGEMANN PHILIPP , KERN MATTHIAS , HORMUTH WOLFGANG ALOIS , GUZMANN MARCUS , KONIG RENE , BERNNAT JENS , KOLIOS GRIGORIOS , GOKE VOLKER , MAASS HANS-JUERGEN , BUKER KARSTEN
Abstract: Винахідстосуєтьсяспособуутилізаціївідхідногогазу, щоміститьвуглеводніі/абодіоксидвуглецю, супровідногогазуі/абобіогазу, якийвідрізняєтьсятим, щовідхіднийгаз, щоміститьвуглеводніі/абодіоксидвуглецю, супровіднийгазі/абобіогазспрямовуютьу реакційнукамеру, ібагатокомпонентнусуміш, якуміститьвідхіднийгаз, супровіднийгазі/абобіогаз, піддаютьперетвореннюу високотемпературнійзоніпритемпературіпонад 1000 °C уприсутностіносіянапродукту формігазовоїсуміші, щоміститьпонад 95 об. % CO, СО2, Н2, Н2О, СН4 і N2, ізалежновідконкретнихобставиннавуглецевміснийтвердийматеріал, принаймні 75 мас. % якоговідноснозагальноїмасивуглецевмісноготвердогоматеріалуосаджуютьнаносій, причомушвидкістьпотокугазовоїсумішівідхідногогазу, супровідногогазуі/абобіогазув реакційнійзоністановитьменшеніж 20 м/с.
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公开(公告)号：AU2013357293B2
公开(公告)日：2017-04-13
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：CA2894958A1
公开(公告)日：2014-06-19
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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