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公开(公告)号:EP2582648A1
公开(公告)日:2013-04-24
申请号:EP11726396.2
申请日:2011-06-14
申请人: BASF SE
发明人: ROHDE, Wolfgang , MIAO, Qiang , BITTERLICH, Stefan , AVERLANT, Gauthier Luc Maurice , WAGNER, Hans-Günter , RÖSSLER-FEIGEL, Beatrice
CPC分类号: C07C2/10 , C07C2/12 , C07C2523/755 , C07C2529/04 , C07C11/02
摘要: In a process for co-oligomerization of olefins, an olefin starting material comprising olefins with n carbon atoms and olefins with 2n carbon atoms is converted over an olefin oligomerization catalyst to a reaction product. The process is performed under such conditions that the conversion of olefins with 2n carbon atoms is less than 10%. Both the co-oligomer with 3n carbon atoms and the olefin with 2n carbon atoms removed from the reaction product have a high hydroformylatability.
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公开(公告)号:EP2582648B1
公开(公告)日:2014-04-30
申请号:EP11726396.2
申请日:2011-06-14
申请人: BASF SE
发明人: ROHDE, Wolfgang , MIAO, Qiang , BITTERLICH, Stefan , AVERLANT, Gauthier Luc Maurice , WAGNER, Hans-Günter , RÖSSLER-FEIGEL, Beatrice
CPC分类号: C07C2/10 , C07C2/12 , C07C2523/755 , C07C2529/04 , C07C11/02
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公开(公告)号:EP2271584B1
公开(公告)日:2013-05-15
申请号:EP09727777.6
申请日:2009-03-13
申请人: BASF SE
CPC分类号: C01B21/22 , C07C45/28 , C07C49/607
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公开(公告)号:EP2389241B1
公开(公告)日:2018-06-06
申请号:EP10701318.7
申请日:2010-01-19
申请人: BASF SE
发明人: TELES, Joaquim, Henrique , RESCH, Peter , RUPPEL, Wilhelm , WEGERLE, Ulrike , GERLINGER, Wolfgang , RÖSSLER-FEIGEL, Beatrice , MEIER, Anton , MÜLLER, Christian
CPC分类号: B01J19/2425 , B01J4/001 , B01J19/006 , B01J2219/00085 , B01J2219/00166 , F28D7/16 , F28F9/0265 , F28F9/0275 , F28F9/0278 , Y02P20/582
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公开(公告)号:EP2389241A2
公开(公告)日:2011-11-30
申请号:EP10701318.7
申请日:2010-01-19
申请人: BASF SE
发明人: TELES, Joaquim, Henrique , RESCH, Peter , RUPPEL, Wilhelm , WEGERLE, Ulrike , GERLINGER, Wolfgang , RÖSSLER-FEIGEL, Beatrice , MEIER, Anton , MÜLLER, Christian
IPC分类号: B01J19/24
CPC分类号: B01J19/2425 , B01J4/001 , B01J19/006 , B01J2219/00085 , B01J2219/00166 , F28D7/16 , F28F9/0265 , F28F9/0275 , F28F9/0278 , Y02P20/582
摘要: The invention relates to a tube bundle reactor having a flat feed dome. Alternatively, the discharge dome can also be designed flat. The flat design reduces the reaction heat developing in the hood in reaction types that take place not only in the tube bundle (non-catalyzed reactions and reactions with homogenously distributed catalyst). Undesired reactions that already take place in the dome due to accumulated heat are thus heavily suppressed, whereby greater selectivity in temperature-sensitive reactions is achieved. Additionally, the temperature distribution within the domes can be precisely controlled. The tube bundle reactor comprises a tube bundle that has a feed end connected to a feed dome of the tube bundle reactor, wherein the feed dome is designed in a flat shape having a cross-sectional surface at the feed end and an inner volume, and the ratio of the inner volume to the cross-sectional surface is less than 0.35 m. The invention is furthermore implemented by a method for operating a tube bundle reactor, comprising: introducing a reactant mixture into a tube bundle and converting at least a portion of the reactant mixture into a product inside the tube bundle. The introduction step comprises: feeding the reactant mixture into an inner space of a feed dome of the tube bundle reactor and forwarding the reactant mixture into a feed end of the tube bundle in the form of a fluid flow. The fluid flow has a cross-sectional surface upon entering the feed end and the inner space of the feed dome through which the fluid flows has an inner volume; wherein the ratio of the inner volume to the cross-sectional surface is less than 0.35 m.
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公开(公告)号:EP2271584A1
公开(公告)日:2011-01-12
申请号:EP09727777.6
申请日:2009-03-13
申请人: BASF SE
CPC分类号: C01B21/22 , C07C45/28 , C07C49/607
摘要: The present invention relates to a process for purifying a gas mixture containing dinitrogen monoxide at least comprising treatment of a gas mixture G-O containing dinitrogen monoxide with a gas mixture G-A being obtained, at least comprising the absorption of the gas mixture G-O in a solvent mixture LM-I with an off-gas stream and a composition Z-A being obtained, and desorption of a gas mixture G-1 from the composition Z-A with a solvent mixture LM-I' being obtained, subsequent condensation of the gas mixture G-A with a liquid composition Z-1 containing dinitrogen monoxide and a gaseous mixture G-K being obtained, wherein the gaseous mixture G-K is recirculated to the process.
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