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11.发明公开
公开(公告)号：EP3744154A1
公开(公告)日：2020-12-02
申请号：EP19701109.1
申请日：2019-01-22
Applicant: BASF SE
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公开(公告)号：EP2931415B1
公开(公告)日：2020-11-18
申请号：EP13814068.6
申请日：2013-12-12
Applicant: BASF SE , Linde GmbH
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13.发明公开VERFAHREN ZUR BLAUSÄURESYNTHESE AUS FORMAMID - PACKUNGSNACHREAKTOR 审中-公开VERFAHREN ZURBLAUSÄURESYNTHESEAUS FORMAMID - PACKUNGSNACHREAKTOR
公开(公告)号：EP2961691A1
公开(公告)日：2016-01-06
申请号：EP14707388.6
申请日：2014-02-28
Applicant: BASF SE
Inventor： BÖHLING, Ralf , SCHIPPER, Michael , BERNNAT, Jens , WEBER, Wilhelm , PETERSEN, Peter
CPC classification number: C01C3/0204 , B01J19/30 , B01J19/32 , B01J2219/30215 , B01J2219/30408 , B01J2219/30416 , B01J2219/30475 , B01J2219/32237 , B01J2219/32408 , B01J2219/32466
Abstract: The invention relates to a method for producing prussic acid by catalytically dehydrating gaseous formamide in at least one main reactor and in a secondary reactor arranged downstream thereof and to the use of a secondary reactor in a method for producing prussic acid by catalytically dehydrating gaseous formamide.
Abstract translation: 在至少一个主反应器和下游后反应器中通过气态甲酰胺的催化脱水制备氢氰酸的方法，以及在通过气态甲酰胺的催化脱水制备氢氰酸的方法中使用后反应器。
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14.发明公开VERFAHREN ZUR VERWERTUNG VON KUPPELGASEN, BEGLEITGASEN UND/ODER BIOGASEN 有权VERFAHREN ZUR VERWERTUNG VON KUPPELGASEN，BEGLEITGASEN UND / ODER BIOGASEN
公开(公告)号：EP2935517A1
公开(公告)日：2015-10-28
申请号：EP13805375.6
申请日：2013-12-13
Applicant: BASF SE , Linde AG , ThyssenKrupp Industrial 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
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-containing and/or carbon dioxide-containing blast furnace gas, accompanying gas and/or biogas, characterized in that hydrocarbon-containing and/or carbon dioxide-containing blast furnace gas, accompanying gas and/or biogas is introduced into a reaction chamber, and the multicomponent mixture present in the blast furnace gas, accompanying gas and/or biogas is converted in a high-temperature zone at temperatures of above 1000°C and in the presence of a support into a product-gas mixture which consists of more than 95% by volume CO, CO
2 , H
2 , H
2 O, CH
4 and N
2 , and optionally into a carbon-containing solid of which more than 75% by weight, based on the total mass of the carbon-containing solid, is deposited onto the support, wherein the flow velocity of the gas mixture blast furnace 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，并且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℃的高温区域和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的载体上。
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15.发明授权
公开(公告)号：EP2935517B1
公开(公告)日：2018-03-21
申请号：EP13805375.6
申请日：2013-12-13
Applicant: BASF SE , ThyssenKrupp Industrial 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
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
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Patent Agency Ranking16.发明公开VERFAHREN ZUR BLAUSÄURESYNTHESE AUS FORMAMID - KATALYSATOR 审中-公开VERFAHREN ZURBLAUSÄURESYNTHESEAUS FORMAMID - KATALYSATOR
公开(公告)号：EP2984037A1
公开(公告)日：2016-02-17
申请号：EP14718544.1
申请日：2014-04-09
Applicant: BASF SE
Inventor： BÖHLING, Ralf , SCHIPPER, Michael , BERNNAT, Jens , WEBER, Wilhelm , PETERSEN, Peter , NEGELE, Anton , DECKERS, Andreas
CPC classification number: C01C3/0204 , B01J21/04 , B01J21/12 , B01J23/745 , B01J35/1009
Abstract: The invention relates to a method for producing hydrocyanic acid by the thermolysis of gaseous formamide in a reactor in the presence of a catalyst, wherein a) the catalyst (i) is an aluminum oxide catalyst, containing - 90 to 100 wt%, preferably 99 to 100 wt%, of aluminum oxide as component A, - 0 to 10 wt%, preferably 0 to 1 wt%, of silicon dioxide as component B, and - 0 to at most 0.1 wt% of iron or compounds containing iron as component C, wherein the total sum of components A, B, and C is 100 wt%, and (ii) has a BET surface area, measured as per DIN ISO 9277 : 2003-05, of 2 /g, and (iii) is tempered at temperatures of > 1400 °C for 1 to 30 h, preferably ≥ 1500 °C for 1 to 30 h, especially preferably at 1500 °C to 1800 °C for 2 to 10 h, and b) the reactor has an inner surface that is inert with respect to the thermolysis of formamide; and use of the catalyst in a method for producing hydrocyanic acid by the thermolysis of gaseous formamide in a reactor that has an inner surface that is inert with respect to the thermolysis of formamide.
Abstract translation: 在催化剂存在下，通过在反应器中热分解气态甲酰胺来制备氢氰酸的方法，其中a）所述催化剂是（i）氧化铝催化剂，其包含90至100重量％，优选99至100重量％ 重量的作为组分A的氧化铝，0至10重量％，优选0至1重量％的作为组分B的二氧化硅和0至不超过0.1重量％的含铁或铁的化合物 作为组分C，其中组分A，B和C的总量为100重量％，并且具有（ii）根据DIN ISO 9277：2003年5月测量的BET表面积<1m 2 / g和 （iii）在> 1400℃的温度下热处理1至30小时，优选≥1500℃，1至30小时，特别优选在1500℃至1800℃，对于2 至10小时，以及b）反应器具有关于甲酰胺热解的惰性的内表面; 以及在反应器中热分解气态甲酰胺制备氢氰酸的方法中使用催化剂，该反应器具有关于甲酰胺热解的惰性的内表面
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公开(公告)号：EP2931415A1
公开(公告)日：2015-10-21
申请号：EP13814068.6
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 , KÖNIG, Rene , BRÜGGEMANN, 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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18.发明公开
公开(公告)号：EP4072720A1
公开(公告)日：2022-10-19
申请号：EP20815801.4
申请日：2020-11-30
Applicant: BASF SE
Inventor： SCHEIFF, Frederik , FLICK, Dieter , SEIDEMANN, Lothar , BERNNAT, Jens , KOLIOS, Grigorios
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19.发明公开
公开(公告)号：EP3833471A1
公开(公告)日：2021-06-16
申请号：EP19748545.1
申请日：2019-08-05
Applicant: BASF SE
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20.发明公开
公开(公告)号：EP2935098A1
公开(公告)日：2015-10-28
申请号：EP13865384.5
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
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).
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