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公开(公告)号：CA3142544A1
公开(公告)日：2020-12-10
申请号：CA3142544
申请日：2020-05-28
Applicant: BASF SE , THYSSENKRUPP AG , THYSSENKRUPP IND SOLUTIONS AG
Inventor： SCHEIFF FREDERIK , KOLIOS GRIGORIOS , BODE ANDREAS
Abstract: The invention relates a method for continuously performing one or more heat-consuming processes, which is characterized in that the at least one heat-consuming process is electrically heated, the maximum temperature in the reaction zone of the heat-consuming process is greater than 500°C, at least 70% of the products of the at least one heat-consuming process are continuously further processed in downstream processes and/or are passed on to a local energy carrier network and the required electrical energy for the at least one heat-consuming process is drawn from an external power grid and from at least one local power source, wherein the at least one local power source is fed at least 50% of its annual energy requirement from at least one local energy carrier network and is fed at most 50% of its annual energy requirement by products from the heat-consuming process, wherein natural gas, naphtha, hydrogen, syngas and/or steam is stored as an energy carrier in the at least one local energy carrier network, wherein the at least one local energy carrier network is fed at least one further product and/or byproduct from at least one further chemical process and wherein the local energy carrier network has a total capacity of at least 5 GWh. The invention also relates to the use of this method as a minute reserve for the public power grid and to the use of local energy carrier networks of chemical sites for the storage of electrical energy.
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公开(公告)号：CA3133519A1
公开(公告)日：2020-09-24
申请号：CA3133519
申请日：2020-03-06
Applicant: BASF SE
Inventor： KOLIOS GRIGORIOS , LAIB HEINRICH , SCHEIFF FREDERIK , ZOELS BERND , KERN MATTHIAS
Abstract: The present invention relates to a gas-tight multilayer composite tube with a heat transfer coefficient of > 500 W/m2/K, which in its structure has, as an inner layer over the cross section of the wall of the composite tube, a non-porous monolithic oxide ceramic, which is enclosed by an outer layer of oxidic fibre-composite ceramic, this outer layer having an open porosity of 5%
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43.发明专利
公开(公告)号：PL2935517T3
公开(公告)日：2018-12-31
申请号：PL13805375
申请日：2013-12-13
Applicant: BASF SE , THYSSENKRUPP IND SOLUTIONS AG
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44.发明专利
公开(公告)号：ES2672331T3
公开(公告)日：2018-06-13
申请号：ES13805375
申请日：2013-12-13
Applicant: BASF SE , THYSSENKRUPP IND SOLUTIONS AG
Inventor： SCHNEIDER CHRISTIAN , BODE ANDREAS , KLINGLER DIRK , MACHHAMMER OTTO , BRÜGGEMANN PHILIPP , KERN MATTHIAS , HORMUTH WOLFGANG ALOIS , GUZMANN MARCUS , KÖNIG RENE , BERNNAT JENS , KOLIOS GRIGORIOS , GOEKE VOLKER , MAASS HANS-JUERGEN , BÜKER KARSTEN
Abstract: Procedimiento para el aprovechamiento de un gas de subproducto, un gas acompañante y/o un biogás que contienen hidrocarburos y que contienen dióxido de carbono, caracterizado porque el gas de subproducto, el gas acompañante y/o el biogás que contienen hidrocarburos y que contienen dióxido de carbono se introducen en un espacio de reacción y la mezcla de múltiples componentes contenida en el gas de subproducto, el gas acompañante y/o el biogás se convierte en una zona de alta temperatura a temperaturas de entre 1100 y 1400 ºC y en presencia de un soporte en una mezcla gaseosa de producto que está constituida en más del 95 % por CO, CO2, H2, H2O, CH4 y N2, en donde se conduce el soporte como lecho móvil por el espacio de reacción y se conduce la mezcla gaseosa de gas de subproducto, gas acompañante y/o biogás en contracorriente con respecto al soporte y se conduce el gas de síntesis caliente formado en la zona de alta temperatura posteriormente en contracorriente por el lecho móvil y se enfría en intercambio de calor directo con éste, ascendiendo la velocidad de flujo de la mezcla gaseosa de gas de subproducto, gas acompañante y/o biogás en la zona de reacción a menos de 20 m/s y enfriándose el gas de síntesis formado en la zona de alta temperatura con > 200 K/s.
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公开(公告)号：RU2650171C2
公开(公告)日：2018-04-09
申请号：RU2015129604
申请日：2013-12-17
Applicant: BASF SE
Inventor： KERN MATTIAS , GLENK FRIDRIKH , KLINGLER DIRK , BODE ANDREAS , KOLIOS GRIGORIOS , SHUNK SHTEFAN , VASSERSHAFF GVIDO , BERNNAT JENS , TSELS BERND , SHMIDT ZABINE , KENIG RENE
Abstract: Изобретениеотноситсяк способупараллельногополученияводорода, монооксидауглеродаи углеродсодержащегопродукта. Описанспособпараллельногополученияводорода, монооксидауглеродаи углеродсодержащегопродукта, вкоторомодинилинесколькоуглеводородовподвергаюттермическойдеструкции, причемпоменьшеймеречастьобразующейсяводородсодержащейгазовойсмесивыводятизреакционнойзоныреакторадеструкциипритемпературеот 800 до 1400°Си превращаютс диоксидомуглеродав содержащуюмонооксидуглеродаи водородгазовуюсмесь. Техническийрезультат: предложенспособпараллельногополученияводорода, монооксидауглеродаи/илитвердогоуглесодержащегопродуктас незначительнымуглекислотнымследомприэкономическиприемлемыхдляхимическойпромышленностиграничныхусловиях. 12 з.п. ф-лы, 6 ил.
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Patent Agency Ranking
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：CA2833915A1
公开(公告)日：2012-11-01
申请号：CA2833915
申请日：2012-04-19
Applicant: BASF SE
Inventor： BALTES CHRISTIAN , KOLIOS GRIGORIOS , RESCH PETER , WEGERLE ULRIKE , MAURER TORSTEN
Abstract: A process for preparing C1-C10-aldehydes by oxidative dehydrogenation of C1-C10-alcohols over a shaped catalyst body obtainable by three-dimensional forming and/or arrangement in the space of silver-containing fibres and/or filaments, characterized in that the mean diameter or the mean diagonal length of an essentially rectangular or square cross section of these silver-containing fibres and/or filaments is in the range from 30 µm to 200 µm.
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公开(公告)号：BR112021024524A2
公开(公告)日：2022-01-18
申请号：BR112021024524
申请日：2020-05-28
Applicant: BASF SE , THYSSENKRUP IND SOLUTIONS AG , THYSSENKRUPP AG
Inventor： BODE ANDREAS , SCHEIFF FREDERIK , KOLIOS GRIGORIOS , BUEKER KARSTEN , LEDUC MARC , ANTWEILER NICOLAI , DALOZ WILLIAM
Abstract: processo integrado e planta conjunta. a presente invenção se refere a um processo integrado contendo as seguintes etapas (i) pirólise de hidrocarbonetos em carbono e hidrogênio, (iia) remoção de pelo menos uma parte do carbono produzido na etapa (i) e, pelo menos parcialmente, processar posteriormente o referido carbono em um eletrodo contendo carbono, (iib) remoção do hidrogênio produzido na etapa (i) e, pelo menos parcialmente, usar o referido hidrogênio para fornecer energia, de preferência energia elétrica ou calor, para a produção de eletrodo na etapa (iia). além disso, a presente invenção se refere a uma planta conjunta contendo (a) pelo menos um reator para processo de pirólise, (b) pelo menos um reator para a produção de eletrodos para um processo de alumínio, (c) uma usina e/ou pelo menos um queimador a gás e, opcionalmente (d) pelo menos um reator para a eletrólise para produzir alumínio.
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公开(公告)号：AU2020286580A1
公开(公告)日：2021-12-23
申请号：AU2020286580
申请日：2020-05-28
Applicant: BASF SE , THYSSENKRUPP AG , THYSSENKRUPP IND SOLUTIONS AG
Inventor： SCHEIFF FREDERIK , KOLIOS GRIGORIOS , BODE ANDREAS
Abstract: The invention relates a method for continuously performing one or more heat-consuming processes, which is characterized in that the at least one heat-consuming process is electrically heated, the maximum temperature in the reaction zone of the heat-consuming process is greater than 500°C, at least 70% of the products of the at least one heat-consuming process are continuously further processed in downstream processes and/or are passed on to a local energy carrier network and the required electrical energy for the at least one heat-consuming process is drawn from an external power grid and from at least one local power source, wherein the at least one local power source is fed at least 50% of its annual energy requirement from at least one local energy carrier network and is fed at most 50% of its annual energy requirement by products from the heat-consuming process, wherein natural gas, naphtha, hydrogen, syngas and/or steam is stored as an energy carrier in the at least one local energy carrier network, wherein the at least one local energy carrier network is fed at least one further product and/or byproduct from at least one further chemical process and wherein the local energy carrier network has a total capacity of at least 5 GWh. The invention also relates to the use of this method as a minute reserve for the public power grid and to the use of local energy carrier networks of chemical sites for the storage of electrical energy.
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公开(公告)号：DE102019002523A1
公开(公告)日：2020-10-08
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 FREDERICK , WECHSUNG ACHIM , WEIKL MARKUS , ZANDER HANS-JÖRG , KOLIOS GRIGORIOS
Abstract: Die Erfindung betrifft einen Reaktor (1) zur Durchführung einer endothermen Reaktion, insbesondere Hochtemperaturreaktion, bei der aus einem Einsatzgas (E) ein Produktgas (P) gewonnen wird, wobei der Reaktor (1) einen Reaktorinnenraum (10) umgibt, wobei der Reaktor (1) dazu konfiguriert ist, in einer Reaktionszone (12) des Reaktorinnenraumes (10) ein Reaktorbett (120) aufweisend eine Vielzahl an Feststoffpartikeln (F) bereitzustellen, wobei der Reaktor (1) weiterhin dazu konfiguriert ist, das Einsatzgas (E) in die Reaktionszone (12) zu führen, wobei der Reaktor (1) zum Heizen des Einsatzgases (E) dazu ausgebildet ist, die Feststoffpartikel (F) in der Reaktionszone (12) zu heizen, so dass das Einsatzgas (E) in der Reaktionszone (12) durch Übertragung von Wärme der Feststoffpartikel (F) auf das Einsatzgas (E) auf eine Reaktionstemperatur heizbar ist, um als Edukt an der endothermen Reaktion zur Erzeugung des Produktgases (P) teilzunehmen, und wobei der Reaktorinnenraum (10) weiterhin eine erste Wärmeintegrationszone (11) aufweist, in der Wärme des in der Reaktionszone (12) erzeugten Produktgases (P) auf in die Reaktionszone (12) zu führende Feststoffpartikel (F) des Reaktorbetts (120) übertragbar ist, und wobei weiterhin der Reaktorinnenraum (10) eine zweite Wärmeintegrationszone (13) aufweist, in der Wärme von aus der Reaktionszone (12) kommenden Feststoffpartikeln (F) des Reaktorbetts (120) zum Vorheizen des Einsatzgases (E) auf das Einsatzgas (E) übertragbar ist. Weiterhin betrifft die Erfindung ein Verfahren, bei dem ein erfindungsgemäßer Reaktor (1) verwendet wird.
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