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公开(公告)号:AU2002361017A1
公开(公告)日:2003-06-17
申请号:AU2002361017
申请日:2002-12-05
Applicant: BASF AG
Inventor: DOBLER WALTER , HAAKE MATHIAS , SIGL MARCUS , MILLER CHRISTIAN
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公开(公告)号:BRPI0507195A
公开(公告)日:2007-06-26
申请号:BRPI0507195
申请日:2005-01-27
Applicant: BASF AG
Inventor: SCHEIDEL JENS , MILLER CHRISTIAN , BAUMANN ROBERT , JUNGKAMP TIM , BARTSCH MICHAEL , HADERLEIN GERD , LUYKEN HERMANN , SIEGEL WOLFGANG , BASSLER PETER
IPC: C07C253/30 , C07C255/07
Abstract: The invention relates to a method for isomerization of pentene nitrile in an educt flow, wherein isomerization is performed on a homogeneously dissolved catalyst.
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公开(公告)号:DE102005014178A1
公开(公告)日:2006-10-05
申请号:DE102005014178
申请日:2005-03-29
Applicant: BASF AG
Inventor: HILL THOMAS , MILLER CHRISTIAN
Abstract: A process is proposed for obtaining a stream of aliphatic hydrocarbons comprising from 4 to 12 carbon atoms per molecule, with an increased proportion of linear alpha-olefins compared to a feed stream of aliphatic hydrocarbons comprising from 4 to 12 carbon atoms per molecule, with a content of linear alpha-olefins, linear internal olefins and dienes, wherein the feed stream is fed to a first distillation zone D 1 having at least 5 theoretical plates, in which the linear alpha-olefins are removed partly or fully as a component of a vapor stream which additionally also comprises the dienes, and at whose lower end a liquid stream is obtained which has been depleted partly or fully of linear alpha-olefins, the liquid stream from the lower end of the first distillation zone D 1 is introduced into a isomerization unit which is equipped with an isomerization catalyst over which the linear internal olefins are isomerized partly or fully to linear alpha-olefins, and the linear alpha-olefins formed in this way are removed as a component of a vapor stream ascending into the first distillation zone D 1, the vapor stream ascending out of the first distillation zone D 1 enters a selective hydrogenation unit comprising a second reactive distillation zone RD 2 in which at least a portion of the dienes are hydrogenated selectively to olefins over a low-isomerization selective hydrogenation catalyst to obtain a vapor stream which is drawn off, condensed fully or partly and drawn off as a product stream with an increased proportion of linear alpha-olefins compared to the feed stream, the distillation zone D 1 and the reactive distillation zone RD 2 being integrated in a single reactive distillation column RDK.
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公开(公告)号:CA2601692A1
公开(公告)日:2006-10-05
申请号:CA2601692
申请日:2006-03-22
Applicant: BASF AG
Inventor: HILL THOMAS , MILLER CHRISTIAN
Abstract: A process is proposed for obtaining a stream of aliphatic hydrocarbons comprising from 4 to 12 carbon atoms per molecule, with an increased proportion of linear alpha-olefins compared to a feed stream of aliphatic hydrocarbons comprising from 4 to 12 carbon atoms per molecule, with a content of linear alpha-olefins, linear internal olefins and dienes, wherein the feed stream is fed to a first distillation zone D 1 having at least 5 theoretical plates, in which the linear alpha-olefins are removed partly or fully as a component of a vapor stream which additionally also comprises the dienes, and at whose lower end a liquid stream is obtained which has been depleted partly or fully of linear alpha-olefins, the liquid stream from the lower end of the first distillation zone D 1 is introduced into a isomerization unit which is equipped with an isomerization catalyst over which the linear internal olefins are isomerized partly or fully to linear alpha-olefins, and the linear alpha-olefins formed in this way are removed as a component of a vapor stream ascending into the first distillation zone D 1, the vapor stream ascending out of the first distillation zone D 1 enters a selective hydrogenation unit comprising a second reactive distillation zone RD 2 in which at least a portion of the dienes are hydrogenated selectively to olefins over a low-isomerization selective hydrogenation catalyst to obtain a vapor stream which is drawn off, condensed fully or partly and drawn off as a product stream with an increased proportion of linear alpha-olefins compared to the feed stream, the distillation zone D 1 and the reactive distillation zone RD 2 being integrated in a single reactive distillation column RDK.
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公开(公告)号:DE50301788D1
公开(公告)日:2006-01-05
申请号:DE50301788
申请日:2003-07-14
Applicant: BASF AG
Inventor: MILLER CHRISTIAN , KAIBEL DR , SIEGEL DR
Abstract: Carrying out reactive distillation in the presence of a heterogeneous catalyst suspended as dispersed phase in the liquid comprises continuously removing a part of the suspension containing the catalyst from the column, treating in a preparation stage, and returning the treated catalyst to the column.
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公开(公告)号:AU2003246692A1
公开(公告)日:2004-02-02
申请号:AU2003246692
申请日:2003-07-14
Applicant: BASF AG
Inventor: KAIBEL GERD , MILLER CHRISTIAN , DOBLER WALTER , DIRNSTEINER THOMAS , HAHN THILO , BREUER KLAUS , AQUILA WERNER , GOBBEL HANS-GEORG
Abstract: A process is described for preparing tetrahydrogeranylacetone in which pseudoionone, geranylacetone and/or dihydrogeranylacetone in a liquid phase, in which particles of a catalyst which is capable of preferentially hydrogenating carbon-carbon double bonds over carbon-oxygen double bonds are suspended, is conducted through a device which inhibits the transport of the catalyst particles in the presence of a hydrogen-containing gas.
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公开(公告)号:DE10226120A1
公开(公告)日:2003-12-24
申请号:DE10226120
申请日:2002-06-12
Applicant: BASF AG
Inventor: SIGL MARCUS , MILLER CHRISTIAN , DOBLER WALTER , HAAKE MATHIAS
IPC: B01J8/00 , B01J8/02 , B01J8/12 , B01J19/24 , B01J21/04 , B01J23/10 , B01J23/92 , B01J35/02 , C07C45/72 , C07C45/74 , C07C49/203
Abstract: The supported catalyst has one or more metal oxides as active components on a carrier for aldol condensation. The catalyst carrier is gamma -aluminum oxide. The active components include one or more oxides of rare earth metals. The concentration of the active components is 5-12 wt.% of the catalyst carrier weight. The active component is preferably yttrium oxide or praseodymium oxide. The condensation column packing (1) is composed of packing sheets (2) with straight kinks (5) forming angled kink surfaces (6). Catalyst particles (4) fill the space (3) between neighboring sheets.
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公开(公告)号:MY139280A
公开(公告)日:2009-09-30
申请号:MYPI20043085
申请日:2004-07-30
Applicant: BASF AG
Inventor: FRAUENKRON MATTHIAS DR , MILLER CHRISTIAN , KRUG THOMAS , EVERS HOLGER DR , MELDER D JOHANN-PETER , ROETTGER RODERICH DR , SIEGERT MARKUS DR , GERLACH TILL DR , NOUWEN JAN DR , DAHLHOFF ELLEN DR
IPC: C07C209/60 , C07C209/64 , C07C211/14
Abstract: PROCESS FOR THE PREPARATION OF ETHYLENAMINES,IN PARTICULAR DIETHYLENETRIAMINE (DETA), BY CONTINUOUS REACTION OF ETHYLENEDIAMINE (EDA) IN THE PRESENCE OF A HETEROGENEOUS CATALYST, WHERE THE REACTION IS CARRIED OUT IN A REACTION COLUMN.
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公开(公告)号:ES2288737T3
公开(公告)日:2008-01-16
申请号:ES05701200
申请日:2005-01-27
Applicant: BASF AG
Inventor: SCHEIDEL JENS , MILLER CHRISTIAN , BAUMANN ROBERT , JUNGKAMP TIM , BARTSCH MICHAEL , HADERLEIN GERD
IPC: C07C253/30 , C07C255/07
Abstract: Procedimiento para la isomerización del pentenonitrilo en una corriente de educto, caracterizado porque la isomerización del cis-2-pentenonitrilo en el trans-3-pentenonitrilo tiene lugar sobre al menos un catalizador disuelto de manera homogénea en la corriente del educto, que es una monoamina o una diamina con 1 hasta 20 átomos de carbono, o un líquido iónico, eligiéndose el líquido iónico entre el grupo constituido por los aductos de ácidos de Brönstedt de substancias nitrogenadas orgánicas.
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公开(公告)号:AT378310T
公开(公告)日:2007-11-15
申请号:AT03763838
申请日:2003-07-14
Applicant: BASF AG
Inventor: GOEBBEL HANS-GEORG , KAIBEL GERD , MILLER CHRISTIAN , DOBLER WALTER , DIRNSTEINER THOMAS , HAHN THILO , BREUER KLAUS , AQUILA WERNER
Abstract: A process is described for preparing tetrahydrogeranylacetone in which pseudoionone, geranylacetone and/or dihydrogeranylacetone in a liquid phase, in which particles of a catalyst which is capable of preferentially hydrogenating carbon-carbon double bonds over carbon-oxygen double bonds are suspended, is conducted through a device which inhibits the transport of the catalyst particles in the presence of a hydrogen-containing gas.
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