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1. 发明授权

EP2739386B1 VERFAHREN ZUR DURCHFÜHRUNG VON KATALYTISCHEN AUTOTHERMEN GASPHASENDEHYDRIERUNGEN IN PRODUKTIONS- UND REGENERIERMODUS 有权
标题翻译：程序催化AUTO SPAS气相生产和脱氢再生模式，并实施
公开(公告)号：EP2739386B1
公开(公告)日：2015-06-10
申请号：EP12740993.6
申请日：2012-08-01
申请人： BASF SE
发明人： OLBERT, Gerhard , WEGERLE, Ulrike , KOLIOS, Grigorios , KOSTOVA, Albena
IPC分类号： B01J19/00 , B01J19/24 , B01J38/14 , C07C5/48 , C07C5/50
CPC分类号： B01J19/2485 , B01J19/0013 , B01J19/0026 , B01J19/0033 , B01J38/14 , B01J2219/00058 , B01J2219/00186 , B01J2219/002 , B01J2219/00202 , B01J2219/00213 , B01J2219/0022 , B01J2219/00229 , B01J2219/1925 , B01J2219/2409 , B01J2219/2416 , B01J2219/2419 , B01J2219/2422 , B01J2219/2443 , C07C5/48 , C07C5/50 , Y02P20/584 , C07C11/08 , C07C15/46 , C07C11/167 , C07C11/06

2. 发明授权

EP2417058B1 VERFAHREN ZUR ELEKTROCHEMISCHEN ABTRENNUNG VON WASSERSTOFF AUS EINEM REAKTIONSGEMISCH 有权
标题翻译：方法从反应混合物中氢的电化学分离
公开(公告)号：EP2417058B1
公开(公告)日：2016-06-01
申请号：EP10711241.9
申请日：2010-03-29
申请人： BASF SE
发明人： COELHO TSOU, Joana , PANCHENKO, Alexander , WENTINK, Annebart, Engbert , AHRENS, Sebastian , HEIDEMANN, Thomas , HUBER, Guenther , KOSTOVA, Albena
IPC分类号： H01M4/92 , H01M8/10 , H01M8/12 , C01B3/50 , H01M8/06
CPC分类号： H01M8/0656 , C01B3/505 , C01B2203/041 , C01B2203/048 , H01M4/92 , H01M4/921 , H01M8/0625 , H01M8/1213 , H01M2008/1095 , H01M2008/1293

3. 发明授权

EP2291341B1 VERFAHREN ZUR ERZEUGUNG VON BENZOL, TOLUOL (UND NAPHTHALIN) AUS C1-C4-ALKANEN UNTER ÖRTLICH GETRENNTER KO-DOSIERUNG VON WASSERSTOFF 有权
标题翻译：用于生产苯，甲苯（和萘）选自C1-C4烷烃UNDER LOCAL SEPARATE KO剂量的氢
公开(公告)号：EP2291341B1
公开(公告)日：2012-03-28
申请号：EP09749856.2
申请日：2009-05-20
申请人： BASF SE
发明人： KIEßLICH, Frank , GRITSCH, Achim , SCHNEIDER, Christian , KOSTOVA, Albena
IPC分类号： C07C2/76
CPC分类号： C07C2/76 , Y02P20/582 , Y02P20/584 , C07C15/00
摘要： The present invention relates to a method for non-oxidative dehydroaromatization of an educt stream comprising C
1 -C
4 aliphates by converting the educt stream to a product stream P comprising an aromatic hydrocarbon, said conversion being done in the presence of a catalyst in a reaction zone 1, and regenerating the catalyst, the activity thereof having been reduced by deposited coke, using a mixture H containing hydrogen in a reaction zone 2, wherein at least a portion of the deposited coke is converted to methane and at least a portion of the resultant methane is fed to reaction zone 1.

4. 发明授权

EP2681178B1 VERFAHREN ZUR AUFARBEITUNG EINES BUTEN- UND/ODER BUTADIEN ENTHALTENDEN STOFFSTROMS 有权
标题翻译：方法处理的丁烯和/或材料含丁二烯流
公开(公告)号：EP2681178B1
公开(公告)日：2014-11-05
申请号：EP12706605.8
申请日：2012-03-02
申请人： BASF SE
发明人： KOSTOVA, Albena , BENFER, Regina , GÖTZ, Jochen , REZAI, Alireza , MORILLO, Aristides , OLBERT, Gerhard , PFAB, Peter , KOLIOS, Grigorios , WEBER, Markus , WECK, Alexander
IPC分类号： C07C7/04 , C07C7/08 , C07C7/11 , C07C11/08 , C07C11/167 , C07C9/10 , B01D3/40
CPC分类号： B01D3/40 , C07C7/04 , C07C7/08 , C07C7/11 , C07C11/16 , C07C11/167

5. 发明公开

EP2291341A1 VERFAHREN ZUR ERZEUGUNG VON BENZOL, TOLUOL (UND NAPHTHALIN) AUS C1-C4-ALKANEN UNTER ÖRTLICH GETRENNTER KO-DOSIERUNG VON WASSERSTOFF 有权
标题翻译：用于生产苯，甲苯（和萘）选自C1-C4烷烃UNDER LOCAL SEPARATE KO剂量的氢
公开(公告)号：EP2291341A1
公开(公告)日：2011-03-09
申请号：EP09749856.2
申请日：2009-05-20
申请人： BASF SE
发明人： KIEßLICH, Frank , GRITSCH, Achim , SCHNEIDER, Christian , KOSTOVA, Albena
IPC分类号： C07C2/76
CPC分类号： C07C2/76 , Y02P20/582 , Y02P20/584 , C07C15/00
摘要： The present invention relates to a method for non-oxidative dehydroaromatization of an educt stream comprising C
1 -C
4 aliphates by converting the educt stream to a product stream P comprising an aromatic hydrocarbon, said conversion being done in the presence of a catalyst in a reaction zone 1, and regenerating the catalyst, the activity thereof having been reduced by deposited coke, using a mixture H containing hydrogen in a reaction zone 2, wherein at least a portion of the deposited coke is converted to methane and at least a portion of the resultant methane is fed to reaction zone 1.

6. 发明公开

EP2909159A2 VERFAHREN ZUR HERSTELLUNG VON CYCLOHEXAN MIT AUS EINEM STEAMCRACKVERFAHREN STAMMENDEN AUSGANGSMATERIALIEN 有权
标题翻译：用于生产用蒸汽CYCLOHEXANE从裂缝过程中获得起始物
公开(公告)号：EP2909159A2
公开(公告)日：2015-08-26
申请号：EP13776829.7
申请日：2013-10-16
申请人： BASF SE
发明人： TSCHIRSCHWITZ, Steffen , WISSEL-STOLL, Kathrin , BÜRKLE, Jochen , KOSTOVA, Albena , SCHMITT, Markus , WLOKA, Veronika , DEUERLEIN, Stephan , BOSCH, Marco , OEHLENSCHLÄGER, Steffen , SCHREIBER, Michael , AVERLANT, Gauthier Luc Maurice , JONI, Joni , PROCHAZKA, Roman , BOCK, Martin , KINDLER, Alois , MALKOWSKY, Daniela , SPUHL, Katharina , BITTERLICH, Stefan , PFEIFFER, Daniel
IPC分类号： C07C5/29 , C07C13/18
CPC分类号： C07C5/10 , C07C5/29 , C07C2523/755 , C07C2527/125 , C07C2601/14 , C07C13/18
摘要： The invention relates to a method for producing cyclohexane by isomerizing a hydrocarbon mixture (KG1) containing methylcyclopentane (MCP) in the presence of a catalyst. The catalyst is preferably an acidic ionic liquid. A flow (S1) originating from a steam cracking process is used as a starting material. The hydrocarbon mixture (KG1) is obtained from said stream (S1) in a device for removing aromatics. The hydrocarbon mixture has a reduced aromatic content in comparison with the flow (S1). (KG1) can also be (nearly) free of aromatics. In dependence on the type and amount of the aromatics remaining in the hydrocarbon mixture (KG1), in particular if benzene is present, a hydrogenation of (KG1) additionally can be performed before the isomerization. Furthermore, additional purification steps can optionally be performed before or after the isomerization or hydrogenation in dependence on the presence of other components of (KG1). Preferably high-purity cyclohexane (in accordance with specifications) is isolated from the hydrocarbon mixture (KG2) arising during the isomerization, wherein the specifications are given, for example, by the use of the cyclohexane for the production of caprolactam known to the person skilled in the art.
摘要翻译：本发明涉及一种通过含异构化在催化剂的存在下的烃混合物（KG1）甲基环戊烷（MCP）生产环己烷。催化剂较好是在酸性离子液体。从蒸汽裂解过程的流程（S1）源自被用作起始材料。烃混合物（KG1）从所述流（S1）在一个设备中获得用于除去芳族化合物。烃混合物具有与所述流（S1）相比较减少的芳族含量。因此（KG1）可以（几乎）不含芳香烃。在剩余在烃混合物（KG1）的芳族化合物的类型和量的依赖性，特别是如果是苯存在的（KG1）氢化另外可在异构化之前进行。进一步，另外的纯化步骤可任选的异构化或氢化之前或之后执行。在依赖（KG1）的其它组分的存在。优选高纯度的环己烷（与规格雅舞蹈）从烃混合物（KG 2）的异构化，worin规格中给出，对于实施例中所产生，通过使用环己烷为已知的本领域技术人员生产己内酰胺的分离的技术人员。

7. 发明授权

EP2506963B1 REAKTOR ZUR DURCHFÜHRUNG VON AUTOTHERMEN GASPHASENDEHYDRIERUNGEN 有权
标题翻译：反应器的实施汽车SPAS气相脱氢
公开(公告)号：EP2506963B1
公开(公告)日：2014-11-05
申请号：EP10784530.7
申请日：2010-11-30
申请人： BASF SE
发明人： KOLIOS, Grigorios , RUPPEL, Wilhelm , WEGERLE, Ulrike , KESSEL, Jasmina , GERLINGER, Wolfgang , MABANDE, Godwin, Tafara, Peter , SCHINDLER, Goetz-Peter , KOSTOVA, Albena , OLBERT, Gerhard , PFAB, Peter
IPC分类号： B01J19/24
CPC分类号： B01J19/2485 , B01J2219/182

8. 发明公开

EP2681178A1 VERFAHREN ZUR AUFARBEITUNG EINES BUTEN- UND/ODER BUTADIEN ENTHALTENDEN STOFFSTROMS 有权
标题翻译： VERFAHREN ZUR AUFARBEITUNG EINES BUTEN - UND / ODER BUTADIEN ENTHALTENDEN STOFFSTROMS
公开(公告)号：EP2681178A1
公开(公告)日：2014-01-08
申请号：EP12706605.8
申请日：2012-03-02
申请人： BASF SE
发明人： KOSTOVA, Albena , BENFER, Regina , GÖTZ, Jochen , REZAI, Alireza , MORILLO, Aristides , OLBERT, Gerhard , PFAB, Peter , KOLIOS, Grigorios , WEBER, Markus , WECK, Alexander
IPC分类号： C07C7/04 , C07C7/08 , C07C7/11 , C07C11/08 , C07C11/167 , C07C9/10
CPC分类号： B01D3/40 , C07C7/04 , C07C7/08 , C07C7/11 , C07C11/16 , C07C11/167
摘要： The invention relates to a process for workup of a stream (1) comprising butene and/or butadiene, butane, hydrogen and/or nitrogen and carbon dioxide, comprising the following steps: (a) absorption of the stream (1) comprising butene and/or butadiene, butane, hydrogen and/or nitrogen, with or without carbon dioxide, with a mixture (5) comprising 80 to 97% by weight of N-methylpyrrolidone and 3 to 20% by weight of water to obtain a stream (9) comprising N-methylpyrrolidone, water, butene and/or butadiene, and butane, with or without carbon dioxide, and a stream (7) comprising hydrogen and/or nitrogen and butane, (b) extractive distillation of the stream (9) comprising N-methylpyrrolidone, water, butene and/or butadiene, and butane, with or without carbon dioxide, with a stream (13) comprising 80 to 97% by weight of N-methylpyrrolidone and 3 to 20% by weight of water to separate the stream (9) comprising N-methylpyrrolidone, water, butene and/or butadiene, and butane, with or without carbon dioxide, into a stream (17) comprising N-methylpyrrolidone, water, butene and/or butadiene, and a stream (15) comprising essentially butane, with or without carbon dioxide, (c) distillation of the stream (17) comprising N-methylpyrrolidone, water, butene and/or butadiene into a stream (23) comprising essentially N-methylpyrrolidone and water, and a stream (21) comprising butene and/or butadiene.
摘要翻译：本发明涉及包含丁烯和/或丁二烯，丁烷，氢气和/或氮气和二氧化碳的物流（1）的处理方法，其包括以下步骤：（a）将包含丁烯和（5）包含80-97重量％的N-甲基吡咯烷酮和3-20重量％的水以获得流（9），所述混合物（5）包含具有或不具有二氧化碳的丁二烯，丁烷，氢和/ ）包含N-甲基吡咯烷酮，水，丁烯和/或丁二烯和丁烷（含有或不含二氧化碳）以及包含氢和/或氮和丁烷的物流（7），（b）物流（9）的萃取蒸馏包含（13）包含80-97重量％的N-甲基吡咯烷酮和3-20重量％的水以分离含有或不含二氧化碳的N-甲基吡咯烷酮，水，丁烯和/或丁二烯和丁烷，包含N-甲基吡咯烷酮，水，丁烯和/或丁二烯和丁烷的物流（9），有或没有汽车（17），包含N-甲基吡咯烷酮，水，丁烯和/或丁二烯，以及基本上包含丁烷的物流（15），其中含有或不含有二氧化碳，（c）蒸馏包含N （23）和包含丁烯和/或丁二烯的物流（21），所述物流（23）基本上包含N-甲基吡咯烷酮和水。

9. 发明公开

EP2506963A1 REAKTOR ZUR DURCHFÜHRUNG VON AUTOTHERMEN GASPHASENDEHYDRIERUNGEN 有权
标题翻译：反应器的实施汽车SPAS气相脱氢
公开(公告)号：EP2506963A1
公开(公告)日：2012-10-10
申请号：EP10784530.7
申请日：2010-11-30
申请人： BASF SE
发明人： KOLIOS, Grigorios , RUPPEL, Wilhelm , WEGERLE, Ulrike , KESSEL, Jasmina , GERLINGER, Wolfgang , MABANDE, Godwin, Tafara, Peter , SCHINDLER, Goetz-Peter , KOSTOVA, Albena , OLBERT, Gerhard , PFAB, Peter
IPC分类号： B01J19/24
CPC分类号： B01J19/2485 , B01J2219/182
摘要： The invention relates to a reactor (1) in the form of a horizontal cylinder for carrying out autothermal gas phase dehydrogenbation of a hydrocarbon-containing gas flow (2) by means of an oxygen-containing gas flow (3), with a reaction mixture being obtained, on a heterogeneous catalyst in the form of a monolith (4), characterized in that the interior of the reactor (1) is divided by a detachable cylindrical or prismatic housing G, which is disposed in the longitudinal direction of the reactor (1), gastight in the circumferential direction and open at both end faces thereof, into an inner area A, having one or a plurality of catalytically active zones (5), in which are provided a packing of monoliths (4) stacked on, adjacent, and above one another, and, in front of each catalytically active zone (5), a mixing zone (6) having fixed installations, and an outer area B disposed coaxially to the inner area A.

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