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公开(公告)号:BR9704644A
公开(公告)日:1998-11-10
申请号:BR9704644
申请日:1997-09-05
Applicant: BASF AG
Inventor: FLICK KLEMENS , HERION CHRISTOF , SCHWAB EKKEHARD , ERDBRUEGGER CHRISTINA F , BROECKER FRANZ JOSEF , MEYER GERALD
IPC: B01J23/56 , B01J23/38 , B01J23/44 , B01J23/50 , B01J23/60 , B01J23/62 , B01J35/06 , B01J37/02 , C07B61/00 , C07C5/05 , C07C5/09 , C07C7/163 , C07C11/02 , C07C11/06 , C07C11/08 , C07C5/02
Abstract: Process for hydrogenating unsaturated 2-8 C hydrocarbons, especially 2-8 C alkynes and/or 4-8 C alkynenes and/or 4-8 C alkadienes into fluid containing them comprises contacting with a catalyst in the presence of hydrogen. The catalyst is produced by applying an active material as catalyst and/or promoter on a gauze or foil as support. Also claimed is a process for catalytic distillation comprising the above hydrogenation with simultaneous distillation or rectification on the catalyst.
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公开(公告)号:DE50111854D1
公开(公告)日:2007-02-22
申请号:DE50111854
申请日:2001-05-09
Applicant: BASF AG
Inventor: MEYER GERALD , KAIBEL GERD , BOHNER GERD , KINDLER KLAUS , ADRIAN TILL , PICKENAECKER KARIN , PAHL MELANIE , HILL THOMAS
IPC: C07C7/08 , C07C11/167 , B01D3/14 , B01D3/40 , C07C5/09 , C07C7/00 , C07C7/163 , C10G7/08 , C10G70/00 , C10G70/02
Abstract: In a process for the work-up of a C4 fraction, comprising the process steps Extractive distillation (I), Selective hydrogenation over a heterogeneous catalyst (II), a crude 1,3-butadiene stream being obtained following process steps (I) and (II) and Distillation of the crude 1,3-butadiene stream for isolating pure 1,3-butadiene (III), the process steps I and II are carried out in a single column or in thermally coupled columns and the process step III is carried out in a second column.
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公开(公告)号:CA2258797C
公开(公告)日:2005-04-05
申请号:CA2258797
申请日:1997-06-16
Applicant: BASF AG
Inventor: BROCKER FRANZ JOSEF , FLICK KLEMENS , POLANEK PETER , KAIBEL GERD , MULLER HANS-JOACHIM , MEYER GERALD , SCHWAB EKKEHARD , FREIRE ERDBRUGGER CRISTINA
IPC: B01D3/00 , B01D59/32 , B01J8/04 , B01J19/24 , B01J19/32 , B01J23/44 , B01J35/02 , B01J35/06 , B01J37/02 , B01J37/34 , C10G49/00 , C10G49/02
Abstract: The use of a catalyst package which can be produced by the vapour deposition and/or sputtering of at least one substance active as a catalyst and/or promotor on fabrics, knitted materials or foils as substrates in a catalytic distillation process in which a heterogeneous-catalytic reaction is combined with simultaneous distillation or rectification on the catalyst package.
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公开(公告)号:AT261339T
公开(公告)日:2004-03-15
申请号:AT01933749
申请日:2001-03-23
Applicant: BASF AG
Inventor: ARNOLD HEIKO DR , FREIRE ERDBRUEGGER CRISTINA , HEIDEMANN THOMAS DR , MEYER GERALD , UNVERRICHT SIGNE , FRENZEL ANDREA DR , WULFF-DOERING JOACHIM , ANSMANN ANDREAS
IPC: B01J35/06 , B01J23/42 , B01J23/44 , B01J23/48 , B01J23/50 , B01J23/70 , B01J23/755 , B01J37/02 , C07B61/00 , C07C5/02 , C07C5/03 , C07C5/08 , C07C7/163 , C07C7/167 , C07C11/04 , C07C11/06 , C07C11/08
Abstract: In a coated catalyst having a core and at least one shell surrounding the core, the core is made up of an inert support material, the shell or shells is/are made up of a porous support substance, with the shell being attached physically to the core, and a catalytically active metal selected from the group consisting of the metals of the 10th and 11th groups of the Periodic Table of the Elements is present in finely divided form or a precursor of the catalytically active metal is present in uniformly distributed form in the shell or shells. The coated catalyst of the present invention is suitable for the reduction of unsaturated hydrocarbons. Here, better selectivities than in the case of previously known coated catalysts can be achieved. A process for producing the coated catalyst is also described.
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公开(公告)号:MX214787B
公开(公告)日:2003-06-19
申请号:MX9706729
申请日:1997-09-04
Applicant: BASF AG
Inventor: FLICK KLEMENS , ERDBRUGGER CRISTINA FREIRE , BROCKER FRANZ JOSEF , MEYER GERALD , SCHWAB EKKEHARD , HERION CHRISTOF
IPC: B01J23/56 , B01J23/38 , B01J23/44 , B01J23/50 , B01J23/60 , B01J23/62 , B01J35/06 , B01J37/02 , C07B61/00 , C07C5/05 , C07C5/09 , C07C7/163 , C07C11/02 , C07C11/06 , C07C11/08
Abstract: Process for hydrogenating unsaturated 2-8 C hydrocarbons, especially 2-8 C alkynes and/or 4-8 C alkynenes and/or 4-8 C alkadienes into fluid containing them comprises contacting with a catalyst in the presence of hydrogen. The catalyst is produced by applying an active material as catalyst and/or promoter on a gauze or foil as support. Also claimed is a process for catalytic distillation comprising the above hydrogenation with simultaneous distillation or rectification on the catalyst.
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公开(公告)号:CZ20023237A3
公开(公告)日:2003-01-15
申请号:CZ20023237
申请日:2001-03-23
Applicant: BASF AG
Inventor: ARNOLD HEIKO , FREIRE ERDBRUGGER CRISTINA , HEIDEMANN THOMAS , MEYER GERALD , UNVERRICHT SIGNE , FRENZEL ANDREA , WULFF-DORING JOACHIM , ANSMANN ANDREAS
IPC: B01J35/06 , B01J23/42 , B01J23/44 , B01J23/48 , B01J23/50 , B01J23/70 , B01J23/755 , B01J37/02 , C07B61/00 , C07C5/02 , C07C5/03 , C07C5/08 , C07C7/163 , C07C7/167 , C07C11/04 , C07C11/06 , C07C11/08 , B01J23/38
Abstract: In a coated catalyst having a core and at least one shell surrounding the core, the core is made up of an inert support material, the shell or shells is/are made up of a porous support substance, with the shell being attached physically to the core, and a catalytically active metal selected from the group consisting of the metals of the 10th and 11th groups of the Periodic Table of the Elements is present in finely divided form or a precursor of the catalytically active metal is present in uniformly distributed form in the shell or shells. The coated catalyst of the present invention is suitable for the reduction of unsaturated hydrocarbons. Here, better selectivities than in the case of previously known coated catalysts can be achieved. A process for producing the coated catalyst is also described.
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公开(公告)号:AT224225T
公开(公告)日:2002-10-15
申请号:AT97929190
申请日:1997-06-16
Applicant: BASF AG
Inventor: BROECKER FRANZ JOSEF , FLICK KLEMENS , FREIRE ERDBRUEGGER CRISTINA , KAIBEL GERD , MEYER GERALD , MUELLER HANS-JOACHIM , POLANEK PETER , SCHWAB EKKEHARD
IPC: B01D3/00 , B01D59/32 , B01J8/04 , B01J19/24 , B01J19/32 , B01J23/44 , B01J35/02 , B01J35/06 , B01J37/02 , B01J37/34 , C10G49/00 , C10G49/02
Abstract: A catalyst packing which can be produced by vapor deposition and/or sputtering of at least one substance active as catalyst and/or promotor onto woven or knitted fabrics or sheets as support material is used in a process for catalytic distillation in which a heterogeneously catalyzed reaction is combined with a simultaneous distillation or rectification over the catalyst packing.
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公开(公告)号:DK0909204T3
公开(公告)日:2002-10-14
申请号:DK97929190
申请日:1997-06-16
Applicant: BASF AG
Inventor: BROECKER FRANZ JOSEF , FLICK KLEMENS , FREIRE ERDBRUEGGER CRISTINA , KAIBEL GERD , MEYER GERALD , MUELLER HANS-JOACHIM , POLANEK PETER , SCHWAB EKKEHARD
IPC: B01D3/00 , B01D59/32 , B01J8/04 , B01J19/24 , B01J19/32 , B01J23/44 , B01J35/02 , B01J35/06 , B01J37/02 , B01J37/34 , C10G49/00 , C10G49/02
Abstract: A catalyst packing which can be produced by vapor deposition and/or sputtering of at least one substance active as catalyst and/or promotor onto woven or knitted fabrics or sheets as support material is used in a process for catalytic distillation in which a heterogeneously catalyzed reaction is combined with a simultaneous distillation or rectification over the catalyst packing.
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公开(公告)号:NO20024648L
公开(公告)日:2002-09-27
申请号:NO20024648
申请日:2002-09-27
Applicant: BASF AG
Inventor: ARNOLD HEIKO , ERDBRUEGGER CRISTINA FREIRE , HEIDEMANN THOMAS , MEYER GERALD , UNVERRICHT SIGNE , FRENZEL ANDREA , WULFF-DOERING JOACHIM , ANSMANN ANDREAS
IPC: B01J35/06 , B01J23/42 , B01J23/44 , B01J23/48 , B01J23/50 , B01J23/70 , B01J23/755 , B01J37/02 , C07B61/00 , C07C5/02 , C07C5/03 , C07C5/08 , C07C7/163 , C07C7/167 , C07C11/04 , C07C11/06 , C07C11/08 , B01J
Abstract: In a coated catalyst having a core and at least one shell surrounding the core, the core is made up of an inert support material, the shell or shells is/are made up of a porous support substance, with the shell being attached physically to the core, and a catalytically active metal selected from the group consisting of the metals of the 10th and 11th groups of the Periodic Table of the Elements is present in finely divided form or a precursor of the catalytically active metal is present in uniformly distributed form in the shell or shells. The coated catalyst of the present invention is suitable for the reduction of unsaturated hydrocarbons. Here, better selectivities than in the case of previously known coated catalysts can be achieved. A process for producing the coated catalyst is also described.
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公开(公告)号:AU8989701A
公开(公告)日:2002-04-02
申请号:AU8989701
申请日:2001-09-19
Applicant: BASF AG
Inventor: KAIBEL GERD , OOST CARSTEN , STROEZEL MANFRED , MEYER GERALD , TRUBENBACH PETER , SARTOR KARL-HEINZ , HENERS JURGEN
Abstract: A process is proposed for the separation of C 5+ cuts by distillation into a low-boiler (A), a medium-boiler (B) and a high-boiler fraction (C) in one or more dividing-wall columns (TK), in which a dividing wall (T) is arranged in the longitudinal direction of the column with formation of an upper, common column region ( 1 ), a lower, common column region ( 6 ), a feed part ( 2, 4 ) with rectifying section ( 2 ) and stripping section ( 4 ), and a withdrawal part ( 3, 5 ) with rectifying section ( 5 ) and stripping section ( 3 ), with feed of the C 5+ cut (A, B, C) into the central region of the feed part ( 2, 4 ), discharge of the high-boiler fraction (C) from the bottom of the column, discharge of the low-boiler fraction (A) via the top of the column, and discharge of the medium-boiler fraction (B) from the central region of the withdrawal part ( 3, 5 ), wherein the dividing ratio of the liquid reflux at the upper end of the dividing wall (T) is set in such a way that the proportion of high-boiling key components in the liquid reflux over the stripping section ( 3 ) of the withdrawal part at the upper end of the dividing wall (T) is from 10 to 80%, preferably from 30 to 50%, of the limit value allowed in the medium-boiler fraction (B), and wherein the heating power in the evaporator at the bottom of the dividing-wall column (TK) is set in such a way that the concentration of the low-boiling key components in the liquid at the lower end of the dividing wall (T) is from 10 to 80%, preferably from 30 to 50%, of the limit value allowed in the medium-boiler fraction (B).
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