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

IPC: C01B3/28 ,  C01B3/30 ,  C01B31/02

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。

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。

公开(公告)号：AU2020375079A1

公开(公告)日：2022-05-19

申请号：AU2020375079

申请日：2020-10-20

Applicant: BASF SE ,  THYSSENKRUPP IND SOLUTIONS AG ,  THYSSENKRUPP AG

Inventor： KOLIOS GRIGORIOS ,  SCHEIFF FREDERIK ,  ANDERLOHR CHRISTOPHER ALEC ,  APPEL HAGEN ,  OLPERT GERHARD ,  ZOELS BERND ,  FLICK DIETER ,  WECHSUNG ACHIM ,  KERN MATTHIAS ,  BUEKER KARSTEN ,  ANTWEILER NICOLAI

IPC: C10J3/30 ,  B01J8/12 ,  C10J3/12 ,  C10J3/72

Abstract: The present invention relates to a method for operating a descending moving bed reactor with flowable granular material, said method comprising the steps of (i) Filling a upper lock-hopper with granular material and/or emptying a lower lock-hopper, (ii) Purging the lock-hoppers with purging gas, (iii) Filling the reaction chamber comprising a descending moving bed from the upper lock-hopper and/or emptying the reaction chamber into the lower lock-hopper, wherein the pressure equalization between the reaction chamber and lock-hopper is achieved with product gas, (iv) optionally Relieving the lock-hoppers and conveying the product gas flow into the product line and (v) Purging the lock-hoppers with purging gas.

公开(公告)号：ZA201400783B

公开(公告)日：2017-11-29

申请号：ZA201400783

申请日：2014-02-03

Applicant: LINDE AG ,  BASF SE

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.

公开(公告)号：AU2013357293A1

公开(公告)日：2015-07-23

申请号：AU2013357293

申请日：2013-12-12

Applicant: BASF SE ,  LINDE AG

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

IPC: B01J19/00 ,  B01J8/00

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.

公开(公告)号：AU2012280624A1

公开(公告)日：2014-02-20

申请号：AU2012280624

申请日：2012-07-05

Applicant: LINDE AG ,  BASF SE

Inventor： MASS HANS-JURGEN ,  GOKE VOLKER ,  MACHHAMMER OTTO ,  GUZMANN MARCUS ,  SCHNEIDER CHRISTIAN ,  HORMUTH WOLFGANG ALOIS ,  BODE ANDREAS ,  KLINGLER DIRK ,  KERN MATTHIAS ,  KOLIOS GRIGORIOS

IPC: C01B3/34 ,  C01B31/02 ,  C01B32/40

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).

公开(公告)号：EP2935098A4

公开(公告)日：2016-10-26

申请号：EP13865384

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 ,  KÖNIG RENE

IPC: C01B3/24 ,  C01B3/38 ,  C01B32/40 ,  C10J3/00 ,  C10K3/02

CPC classification number: C01B3/24 ,  C01B3/38 ,  C01B31/18 ,  C01B32/40 ,  C01B2203/0238 ,  C01B2203/0272 ,  C01B2203/0283 ,  C01B2203/1235 ,  C10J3/06 ,  C10K3/026 ,  Y02P20/129 ,  Y02P20/146

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

IPC: B32B18/00 ,  C01B3/02 ,  C01C3/02 ,  C10G9/16 ,  F16L9/00 ,  F28F1/40

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%

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

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

IPC: C10B55/10 ,  C01B3/34

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

IPC: C10B55/10 ,  C01B3/34

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.