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公开(公告)号:CA2629480A1
公开(公告)日:2007-05-18
申请号:CA2629480
申请日:2006-11-14
Applicant: BASF AG
Inventor: HESSE MICHAEL , MUELLER ULRICH , SCHUBERT MARKUS , ASSMANN JENS , DESBOIS PHILIPPE , URTEL MELANIE
Abstract: The invention relates to a porous organo-metallic skeleton material for accommodating at least one substance. The skeleton material contains at least one at least bidentate organic compound that is coordinatively bound to at least one metal ion, whereby the skeleton material has, at least in part, pores that contain a polymer, which is suited for adsorbing a substance. The invention also relates to a method for producing the skeleton material, to a method for accommodating at least one substance by the skeleton material, and to the use of the skeleton material, in particular, for storing, separating, controlled release or chemically converting an accommodated substance.
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公开(公告)号:DE102005053430A1
公开(公告)日:2007-05-16
申请号:DE102005053430
申请日:2005-11-09
Applicant: BASF AG
Inventor: SCHUBERT MARKUS , MUELLER ULRICH , RUETZ ROGER , HATSCHER STEPHAN
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公开(公告)号:DE102005023857A1
公开(公告)日:2006-11-30
申请号:DE102005023857
申请日:2005-05-24
Applicant: BASF AG
Inventor: MUELLER ULRICH , HESSE MICHAEL , PUETTER HERMANN , SCHUBERT MARKUS , GUZMANN MARCUS , HUFF JUERGEN
Abstract: The present invention relates to suspensions for odor reduction comprising a porous metal-organic framework material in a liquid, and also atomizer and methods for odor reduction using the suspensions. The invention likewise relates to the use of the suspensions for odor reduction.
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公开(公告)号:DE102004061238A1
公开(公告)日:2006-06-22
申请号:DE102004061238
申请日:2004-12-20
Applicant: BASF AG
Inventor: MUELLER ULRICH , HESSE MICHAEL , PUETTER HERMANN , SCHUBERT MARKUS , MIRSCH DETLEF
Abstract: Method for the enrichment of methane in methane containing gas mixtures comprises contacting the gas mixture with at least a sorbent containing a porous metal-organic structure material containing at least one coordinative metal ion bound to a bidentate organic compound.
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公开(公告)号:CA2557273A1
公开(公告)日:2005-09-09
申请号:CA2557273
申请日:2005-02-24
Applicant: BASF AG
Inventor: BOEHM VOLKER , POPLOW FRANK , SCHUBERT MARKUS , WEICHERT CHRISTIAN , BRODHAGEN ANDREAS , STEPHAN JUERGEN , BORCHERT HOLGER
Abstract: The invention relates to a supported catalyst consisting of a support (T) comprising at least 75 wt. % Al2O3 and rhenium compounds as the active component (A). According to the invention, the maximum distribution function of the pore diameter lies in the mesopore range between 0.008 and 0.050 ~m.
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公开(公告)号:DE10319439A1
公开(公告)日:2004-11-18
申请号:DE10319439
申请日:2003-04-30
Applicant: BASF AG
Inventor: SCHUBERT MARKUS , HESSE MICHAEL , STEPHAN JUERGEN , BOEHM VOLKER , BRODHAGEN ANDREAS , POPLOW FRANK , SINNER-LANG MARTINA , DIEHLMANN UWE , COX GERHARD , PFEIFER JOCHEN
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公开(公告)号:DE10225926A1
公开(公告)日:2003-12-24
申请号:DE10225926
申请日:2002-06-11
Applicant: BASF AG
Inventor: HESSE MICHAEL , SCHLITTER STEPHAN , BORCHERT HOLGER , SCHUBERT MARKUS , ROESCH MARKUS , BOTTKE NILS , FISCHER ROLF-HARTMUTH , WECK ALEXANDER , WINDECKER GUNTHER , HEYDRICH GUNNAR
IPC: C07B61/00 , C07C29/149 , C07C31/20 , C07C29/132 , C07D307/20 , C07D307/32
Abstract: The present invention relates to a process for preparing optionally alkyl-substituted 1,4-butanediol by two-stage catalytic hydrogenation in the gas phase of C 4 -dicarboxylic acids and/or of derivatives thereof having the following steps: a) introducing a gas stream of a C 4 -dicarboxylic acid or of a derivative thereof at from 200 to 300° C. and from 10 to 100 bar into a first reactor or into a first reaction zone of a reactor and catalytically hydrogenating it in the gas phase to a product which contains mainly optionally alkyl-substituted gamma-butyrolactone; b) introducing the product stream obtained in this way into a second reactor or into a second reaction zone of a reactor at a temperature of from 140° C. to 260° C. and catalytically hydrogenating it in the gas phase to optionally alkyl-substituted 1,4-butanediol; steps a) and b) being carried out at the same pressure; c) removing the desired product from intermediates, by-products and any unconverted reactants; d) optionally recycling unconverted intermediates into one or both hydrogenation stages, said hydrogenation stages each using a catalyst which comprises =5% by weight, preferably from 5 to 95% by weight, in particular from 20 to 90% by weight, of an oxidic support, and the product mixture removed from the first hydrogenation stage being introduced without further purification into the second hydrogenation stage.
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公开(公告)号:AU2003246407A1
公开(公告)日:2003-12-22
申请号:AU2003246407
申请日:2003-06-10
Applicant: BASF AG
Inventor: WECK ALEXANDER , WINDECKER GUNTHER , HEYDRICH GUNNAR , HESSE MICHAEL , SCHLITTER STEPHAN , BORCHERT HOLGER , SCHUBERT MARKUS , ROSCH MARKUS , BOTTKE NILS , FISCHER ROLF-HARTMUTH
IPC: C07B61/00 , C07C29/149 , C07C31/20
Abstract: The present invention relates to a process for preparing optionally alkyl-substituted 1,4-butanediol by two-stage catalytic hydrogenation in the gas phase of C 4 -dicarboxylic acids and/or of derivatives thereof having the following steps: a) introducing a gas stream of a C 4 -dicarboxylic acid or of a derivative thereof at from 200 to 300° C. and from 10 to 100 bar into a first reactor or into a first reaction zone of a reactor and catalytically hydrogenating it in the gas phase to a product which contains mainly optionally alkyl-substituted gamma-butyrolactone; b) introducing the product stream obtained in this way into a second reactor or into a second reaction zone of a reactor at a temperature of from 140° C. to 260° C. and catalytically hydrogenating it in the gas phase to optionally alkyl-substituted 1,4-butanediol; steps a) and b) being carried out at the same pressure; c) removing the desired product from intermediates, by-products and any unconverted reactants; d) optionally recycling unconverted intermediates into one or both hydrogenation stages, said hydrogenation stages each using a catalyst which comprises =5% by weight, preferably from 5 to 95% by weight, in particular from 20 to 90% by weight, of an oxidic support, and the product mixture removed from the first hydrogenation stage being introduced without further purification into the second hydrogenation stage.
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公开(公告)号:CA2584235C
公开(公告)日:2012-09-11
申请号:CA2584235
申请日:2005-10-13
Applicant: BASF AG
Inventor: STEPHAN JUERGEN , BRODHAGEN ANDREAS , SCHUBERT MARKUS , POPLOW FRANK , ROEPER MICHAEL , HILL THOMAS
IPC: C07C5/05 , C07C6/04 , C07C11/08 , C07C11/10 , C07C11/107
Abstract: The invention relates to a C4-olefin mixture having a 1,3-butadiene content of between 100 and 500 ppm and a 1,2-diene content of less than 10 ppm. The invention also relates to a method for producing said C4-olefin mixture, and to the use thereof in a metathesis reaction for producing 2-pentene and/or 3-hexene.
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公开(公告)号:MX2007010290A
公开(公告)日:2008-03-04
申请号:MX2007010290
申请日:2006-02-24
Applicant: BASF AG
Inventor: HEIDEMANN THOMAS , STEPHAN JURGEN , SCHUBERT MARKUS , POPLOW FRANK , DIEHLMANN UWE , MALTRY MICHAELA
Abstract: La invencion se refiere a un proceso para producir un compuesto o una mezcla de compuestos que tienen un doble enlace C-C o triple enlace C-C no aromatico (compuesto A) a partir de otro compuesto o una mezcla de otros compuestos que tienen un doble enlace C-C o triple enlace C-C no aromatico (compuesto B), que comprende I. una etapa (I) que consiste en liberar al compuesto (B) de impurezas poniendo en contacto dichas impurezas con un agente de adsorcion que comprende al menos 3% en peso de oxido de aluminio y activandolos a temperaturas de 450 a 1000 degree C (agente de adsorcion X) y II. una etapa (II), que consiste en eliminar las impurezas del compuesto (B) de acuerdo con la etapa (I) y poniendo dicho compuesto B en contacto con un catalizador de metatesis bajo condiciones usuales para una reaccion de metatesis.
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