公开(公告)号：US20160068390A1

公开(公告)日：2016-03-10

申请号：US14653482

申请日：2013-12-13

Applicant: BASF SE ,  LINDE AG ,  THYSSENKRUPP INDUSTRIAL SOLUTIONS AG

Inventor： Christian SCHNEIDER ,  Andreas BODE ,  Dirk KLINGLER ,  Otto MACHHAMMER ,  Philipp BRUEGGEMANN ,  Matthias KERN ,  Wolfgang Alois HORMUTH ,  Marcus GUZMANN ,  Rene KOENIG ,  Jens BERNNAT ,  Grigorios KOLIOS ,  Volker GOEKE ,  Hans-Juergen MAASS ,  Karsten BUEKER

IPC: C01B3/34

CPC classification number: C01B3/344 ,  C01B2203/0222 ,  C01B2203/0238 ,  C01B2203/0244 ,  C01B2203/06 ,  C01B2203/0844 ,  C01B2203/085 ,  C01B2203/0855 ,  C01B2203/0861 ,  C01B2203/0883 ,  C01B2203/1235

Abstract: The invention relates to a process for utilizing a hydrocarbon-comprising and/or carbon dioxide-comprising coproduct gas, accompanying gas and/or biogas, wherein hydrocarbon-comprising and/or carbon dioxide-comprising coproduct gas, accompanying gas and/or biogas is introduced into a reaction space and the multicomponent mixture comprised in the coproduct gas, accompanying gas and/or biogas is converted in a high-temperature zone at temperatures of more than 1000° C. and in the presence of a carrier into a product gas mixture which comprises more than 95% by volume of CO, CO2, H2, H2O, CH4 and N2 and optionally into a carbon-comprising solid which is deposited to an extent of at least 75% by weight, based on the total mass of the carbon-comprising solid, on the carrier where the flow velocity of the gas mixture of coproduct gas, accompanying gas and/or biogas in the reaction zone is less than 20 m/s.

Abstract translation: 本发明涉及一种利用含烃和/或二氧化碳的副产物气体，伴随的气体和/或生物气体的方法，其中含烃和/或二氧化碳的副产物气体，伴随的气体和/或生物气体是 引入到反应空间中，包含在副产气体中的伴随气体和/或生物气体的多组分混合物在高于1000℃的温度的高温区域中并且在载体存在下转化成产物气体混合物 其包含超过95体积％的CO，CO 2，H 2，H 2 O，CH 4和N 2，并任选地加入到基于碳的总质量至少75重量％的程度沉积的含碳固体 在载体上，反应区中副产物气体，伴随气体和/或生物气体的气体混合物的流速小于20m / s。

公开(公告)号：US20240391765A1

公开(公告)日：2024-11-28

申请号：US18698377

申请日：2022-09-26

Applicant: BASF SE

Inventor： Grigorios KOLIOS ,  Andreas BODE ,  Johannes BODE ,  Laila Raquel PASIN E MATOS ,  Michael REITZ ,  Frederik SCHEIFF ,  David SCHLERETH

IPC: C01B3/26 ,  B01J8/02

Abstract: The present invention provides a process of producing hydrogen comprising introducing methane and/or other light hydrocarbons into a reaction chamber and reacting said gases in said reaction chamber in a bed of solid carbonaceous materials to give hydrogen, wherein said carbonaceous materials are macro-structured carbonaceous materials, wherein the porosity of the carbonaceous material is in the range of 30 to 70 vol.-% and the carbonaceous material contains a content of carbon of 99 wt.-% to 100 wt.-% and a content of alkaline-earth metals, transition metals and metalloids of 0 and 1 wt.-% in relation to the total mass of the solid carbonaceous material, wherein the iron content is between 0 and 0.5 wt.-%, the magnesium content is between 0 and 0.005 wt.-%, the manganese content is between 0 and 0.01 wt.-%, the silicon content is between 0 and 0.01 wt.-% and the nickel content is between 0 and 0.025 wt.-%. In addition, the present invention provides the use of said carbonaceous materials as carrier material in bed reactors.

公开(公告)号：US20150321912A1

公开(公告)日：2015-11-12

申请号：US14651862

申请日：2013-12-12

Applicant: BASF SE ,  LINDE AG

Inventor： Otto MACHHAMMER ,  Wolfgang Alois HORMUTH ,  Christian SCHNEIDER ,  Andreas BODE ,  Volker GOEKE ,  Hans-Juergen MASS ,  Matthias KERN ,  Dirk KLINGLER ,  Rene KOENIG ,  Philipp BRUEGGEMANN ,  Jens BERNNAT ,  Grigorios KOLIOS

IPC: C01B3/28

CPC classification number: C01B3/28 ,  B01J8/00 ,  B01J19/00 ,  B01J2208/00415 ,  B01J2219/00135 ,  C01B2203/0272 ,  C01B2203/0866

Abstract: The invention relates to a method of carrying out heat-consuming processes, wherein the total energy required averaged over a year for the heat-consuming process originates from at least two different energy sources, where one of the energy sources is an electric energy source whose power varies in the range from 0 to 100% of the total power required, and three different energy modes can individually provide the total power required for the heat-consuming process: (i) exclusively electric energy, (ii) a mixture of electric energy and at least one further nonelectric energy source or (iii) exclusively nonelectric energy, where the changeover time in which the change from one energy mode to another energy mode is completed is not more than 30 minutes.

Abstract translation: 本发明涉及一种进行耗热过程的方法，其中对于耗热过程而言，平均一年以上的总能量源自至少两个不同的能源，其中一个能量源是电能源， 功率在所需总功率的0至100％的范围内变化，并且三种不同的能量模式可以单独地提供耗散过程所需的总功率：（i）专用电能，（ii）电能的混合 和至少一个另外的非电能源，或者（iii）唯一的非电能，其中从一个能量模式到另一个能量模式的改变的转换时间不超过30分钟。

公开(公告)号：US20160052785A1

公开(公告)日：2016-02-25

申请号：US14827496

申请日：2015-08-17

Applicant: LINDE AKTIENGESELLSCHAFT ,  BASF SE

Inventor： Hans-Jurgen Maass ,  Otto MACHHAMMER ,  Andreas BODE ,  Grigorios KOLIOS

IPC: C01B3/30

CPC classification number: C01B3/30 ,  C01B3/24 ,  C01B3/28 ,  C01B32/40 ,  C01B2203/0216 ,  C01B2203/0272 ,  C01B2203/061 ,  C01B2203/062 ,  C01B2203/0822 ,  C01B2203/0838 ,  C01B2203/085 ,  C01B2203/1235 ,  C01B2203/148 ,  C01B2203/84 ,  C10J3/18 ,  C10J3/20 ,  C10K3/026 ,  Y02P20/128 ,  Y02P20/129 ,  Y02P20/146

Abstract: The invention relates to a process for producing synthesis gas, in which carbon and hydrogen are obtained from hydrocarbon by thermal decomposition. At least a portion of the carbon obtained by the thermal decomposition is reacted, and at least a portion of the hydrogen obtained is reacted with carbon dioxide by a reverse water-gas shift reaction to give carbon monoxide and water. Carbon obtained by the thermal hydrocarbon decomposition is used as fuel in a power plant operation wherein the carbon is combusted to produce electrical power, and carbon dioxide formed in the combustion of the carbon is used in the reverse water-gas shift reaction.

Abstract translation: 本发明涉及一种生产合成气的方法，其中通过热分解由烃获得碳和氢。 使通过热分解获得的碳的至少一部分反应，并且通过反向水煤气变换反应将所获得的氢的至少一部分与二氧化碳反应，得到一氧化碳和水。 通过热分解碳获得的碳用作发电厂操作中的燃料，其中碳被燃烧以产生电力，并且在反向水煤气变换反应中使用在碳的燃烧中形成的二氧化碳。

公开(公告)号：US20150336795A1

公开(公告)日：2015-11-26

申请号：US14652346

申请日：2013-12-17

Applicant: BASF SE

Inventor： Matthias KERN ,  Friedrich GLENK ,  Dirk KLINGLER ,  Andreas BODE ,  Grigorios KOLIOS ,  Stephan SCHUNK ,  Guido WASSERSCHAFF ,  Jens BERNNAT ,  Bernd ZOELS ,  Sabine SCHMIDT ,  Rene KOENIG

IPC: C01B3/38 ,  C01B3/24

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

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).

Abstract translation: 本发明涉及一种氢气，一氧化碳和含碳产物的并行制备方法，其中一种或多种烃被热分解，形成的热分解气体的至少一部分从分解反应器的反应区域中取出 在800至1400℃的温度下进行反应，并与二氧化碳反应形成包含一氧化碳和氢气（合成气体）的气体混合物。