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公开(公告)号:BG64090B1
公开(公告)日:2003-12-31
申请号:BG10333999
申请日:1999-04-15
Applicant: BASF AG
Inventor: REHFINGER ALWIN , GANN MARTIN , MERKL ROBERT , SCHMITT RUDIGER
IPC: B01J31/24 , C07C27/12 , C07C29/32 , C07C29/44 , C07C29/50 , C07C31/135 , C07C33/02 , C07C33/03 , C07C33/035 , C07C35/08 , C07C45/33 , C07C45/51 , C07C49/403 , C07C49/603
Abstract: By the method oxidation products of cyclohexane are produced by catalytic oxidation with oxygen-containing gas in liquid phase where the gases enter at least one reaction zone, essentially evently, in contact with liquid cyclohexane. The liquid cyclohexane and the oxygen-containing gases are introduced in a counterflow across the reaction zone. 10 claims
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公开(公告)号:ES2164372T3
公开(公告)日:2002-02-16
申请号:ES97948761
申请日:1997-10-17
Applicant: BASF AG
Inventor: REHFINGER ALWIN , GANN MARTIN , MARKL ROBERT , SCHMITT RUDIGER
IPC: B01J31/24 , C07C27/12 , C07C29/32 , C07C29/44 , C07C29/50 , C07C31/135 , C07C33/02 , C07C33/03 , C07C33/035 , C07C35/08 , C07C45/33 , C07C45/51 , C07C49/403 , C07C49/603
Abstract: PCT No. PCT/EP97/05740 Sec. 371 Date Apr. 14, 1999 Sec. 102(e) Date Apr. 14, 1999 PCT Filed Oct. 17, 1997 PCT Pub. No. WO98/17612 PCT Pub. Date Apr. 30, 1998In a process for preparing oxidation products of cyclohexane by catalytic oxidation with oxygen-containing gases in the liquid phase, where the gases are brought into contact essentially uniformly with the liquid cyclohexane in a reaction zone, liquid cyclohexane and the oxygen-containing gases are passed in countercurrent through the reaction zone.
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公开(公告)号:DE59704612D1
公开(公告)日:2001-10-18
申请号:DE59704612
申请日:1997-10-17
Applicant: BASF AG
Inventor: REHFINGER ALWIN , GANN MARTIN , MAERKL ROBERT , SCHMITT RUEDIGER
IPC: B01J31/24 , C07C27/12 , C07C29/32 , C07C29/44 , C07C29/50 , C07C31/135 , C07C33/02 , C07C33/03 , C07C33/035 , C07C35/08 , C07C45/33 , C07C45/51 , C07C49/403 , C07C49/603
Abstract: PCT No. PCT/EP97/05740 Sec. 371 Date Apr. 14, 1999 Sec. 102(e) Date Apr. 14, 1999 PCT Filed Oct. 17, 1997 PCT Pub. No. WO98/17612 PCT Pub. Date Apr. 30, 1998In a process for preparing oxidation products of cyclohexane by catalytic oxidation with oxygen-containing gases in the liquid phase, where the gases are brought into contact essentially uniformly with the liquid cyclohexane in a reaction zone, liquid cyclohexane and the oxygen-containing gases are passed in countercurrent through the reaction zone.
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公开(公告)号:SK46099A3
公开(公告)日:2000-04-10
申请号:SK46099
申请日:1997-10-17
Applicant: BASF AG
Inventor: REHFINGER ALWIN , GANN MARTIN , MARKL ROBERT , SCHMITT RUDIGER
IPC: B01J31/24 , C07C27/12 , C07C29/32 , C07C29/44 , C07C29/50 , C07C31/135 , C07C33/02 , C07C33/03 , C07C33/035 , C07C35/08 , C07C45/33 , C07C45/51 , C07C49/403 , C07C49/603
Abstract: PCT No. PCT/EP97/05740 Sec. 371 Date Apr. 14, 1999 Sec. 102(e) Date Apr. 14, 1999 PCT Filed Oct. 17, 1997 PCT Pub. No. WO98/17612 PCT Pub. Date Apr. 30, 1998In a process for preparing oxidation products of cyclohexane by catalytic oxidation with oxygen-containing gases in the liquid phase, where the gases are brought into contact essentially uniformly with the liquid cyclohexane in a reaction zone, liquid cyclohexane and the oxygen-containing gases are passed in countercurrent through the reaction zone.
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公开(公告)号:CZ124399A3
公开(公告)日:1999-12-15
申请号:CZ124399
申请日:1997-10-17
Applicant: BASF AG
Inventor: REHFINGER ALWIN , GANN MARTIN , MARKL ROBERT , SCHMITT RUDIGER
IPC: B01J31/24 , C07C27/12 , C07C29/32 , C07C29/44 , C07C29/50 , C07C31/135 , C07C33/02 , C07C33/03 , C07C33/035 , C07C35/08 , C07C45/33 , C07C45/51 , C07C49/403 , C07C49/603
Abstract: PCT No. PCT/EP97/05740 Sec. 371 Date Apr. 14, 1999 Sec. 102(e) Date Apr. 14, 1999 PCT Filed Oct. 17, 1997 PCT Pub. No. WO98/17612 PCT Pub. Date Apr. 30, 1998In a process for preparing oxidation products of cyclohexane by catalytic oxidation with oxygen-containing gases in the liquid phase, where the gases are brought into contact essentially uniformly with the liquid cyclohexane in a reaction zone, liquid cyclohexane and the oxygen-containing gases are passed in countercurrent through the reaction zone.
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公开(公告)号:DE19643154A1
公开(公告)日:1998-04-23
申请号:DE19643154
申请日:1996-10-18
Applicant: BASF AG
Inventor: REHFINGER ALWIN DR , GANN MARTIN , MAERKL ROBERT DR , SCHMITT RUEDIGER
IPC: B01J31/24 , C07C27/12 , C07C29/32 , C07C29/44 , C07C29/50 , C07C31/135 , C07C33/02 , C07C33/03 , C07C33/035 , C07C35/08 , C07C45/33 , C07C45/51 , C07C49/403 , C07C49/603 , C07C49/303
Abstract: The invention concerns a process for preparing oxidation products from cyclohexane by catalytic oxidation with oxygenous gases in the liquid phase. In a reaction zone the gases are brought substantially uniformly into contact with the oxygenous gases, and liquid cyclohexane and the oxygenous gases are passed in counterflow through the reaction zone.
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公开(公告)号:PL1611184T3
公开(公告)日:2007-02-28
申请号:PL04721865
申请日:2004-03-19
Applicant: BASF AG
Inventor: DEININGER JÜRGEN , DEMETER JÜRGEN , KORY GAD , SÖTJE OLIVER , WINTERLING HELMUT , ZEHNER PETER , HEEGER MICHAEL , GANN MARTIN , POLT AXEL , TREULING ULRICH , WEINLE WERNER
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公开(公告)号:DE502004001613D1
公开(公告)日:2006-11-09
申请号:DE502004001613
申请日:2004-03-19
Applicant: BASF AG
Inventor: DEININGER JUERGEN , DEMETER JUERGEN , KORY GAD , SOETJE OLIVER , WINTERLING HELMUT , ZEHNER PETER , HEEGER MICHAEL , GANN MARTIN , POLT AXEL , TREULING ULRICH , WEINLE WERNER
Abstract: Polyamides, oligomers thereof or mixtures thereof, if required with further reaction products, are prepared by reacting aminonitriles or dinitriles and diamines or a mixture containing aminonitrile, dinitrile and diamine, and, if required, further polyamide-forming monomers and/oligomers with water in a reactor ( 1 ) having a vertically oriented longitudinal axis, by a process in which, in the reactor ( 1 ), the reaction product is removed from the bottom and ammonia formed and any further low molecular weight compounds formed and water are taken off via the top ( 2 ), wherein the reactor ( 1 ) has at least two chambers ( 4 ) arranged one on top of the other in the longitudinal direction, the chambers ( 4 ) being separated from one another by liquid-tight trays ( 5 ), each chamber ( 4 ) being connected by a liquid overflow ( 6 ) to the chamber ( 4 ) directly underneath and a liquid product stream being taken off by the liquid overflow ( 6 ) of the lowermost chamber ( 4 ), the gas space ( 7 ) above the liquid level in each chamber ( 4 ) being connected to the chamber ( 4 ) arranged directly above in each case by one or more conduit pipes ( 8 ) which in each case opens or open into a gas distributor ( 9 ) having orifices ( 11 ) for gas exit below the liquid level, and comprising in each case at least one baffle plate ( 12 ) which is arranged vertically around each gas distributor ( 9 ) and whose upper end terminates below the liquid level and whose lower end terminates above the liquid-tight tray ( 5 ) of the chamber ( 4 ) and which separates each chamber ( 4 ) into one or more gassed ( 13 ) and into one or more ungassed ( 14 ) spaces.
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公开(公告)号:AT340819T
公开(公告)日:2006-10-15
申请号:AT04721865
申请日:2004-03-19
Applicant: BASF AG
Inventor: DEININGER JUERGEN , DEMETER JUERGEN , KORY GAD , SOETJE OLIVER , WINTERLING HELMUT , ZEHNER PETER , HEEGER MICHAEL , GANN MARTIN , POLT AXEL , TREULING ULRICH , WEINLE WERNER
Abstract: Polyamides, oligomers thereof or mixtures thereof, if required with further reaction products, are prepared by reacting aminonitriles or dinitriles and diamines or a mixture containing aminonitrile, dinitrile and diamine, and, if required, further polyamide-forming monomers and/oligomers with water in a reactor ( 1 ) having a vertically oriented longitudinal axis, by a process in which, in the reactor ( 1 ), the reaction product is removed from the bottom and ammonia formed and any further low molecular weight compounds formed and water are taken off via the top ( 2 ), wherein the reactor ( 1 ) has at least two chambers ( 4 ) arranged one on top of the other in the longitudinal direction, the chambers ( 4 ) being separated from one another by liquid-tight trays ( 5 ), each chamber ( 4 ) being connected by a liquid overflow ( 6 ) to the chamber ( 4 ) directly underneath and a liquid product stream being taken off by the liquid overflow ( 6 ) of the lowermost chamber ( 4 ), the gas space ( 7 ) above the liquid level in each chamber ( 4 ) being connected to the chamber ( 4 ) arranged directly above in each case by one or more conduit pipes ( 8 ) which in each case opens or open into a gas distributor ( 9 ) having orifices ( 11 ) for gas exit below the liquid level, and comprising in each case at least one baffle plate ( 12 ) which is arranged vertically around each gas distributor ( 9 ) and whose upper end terminates below the liquid level and whose lower end terminates above the liquid-tight tray ( 5 ) of the chamber ( 4 ) and which separates each chamber ( 4 ) into one or more gassed ( 13 ) and into one or more ungassed ( 14 ) spaces.
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公开(公告)号:CA2519816A1
公开(公告)日:2004-10-07
申请号:CA2519816
申请日:2004-03-19
Applicant: BASF AG
Inventor: DEMETER JURGEN , DEININGER JURGEN , WINTERLING HELMUT , HEEGER MICHAEL , ZEHNER PETER , GANN MARTIN , KORY GAD , SOTJE OLIVER , POLT AXEL , TREULING ULRICH , WEINLE WERNER
Abstract: The invention relates to a method for producing polyamides, their oligomers or mixtures thereof, optionally containing other reaction products, by reacting aminonitriles or dinitriles and diamines or a mixture containing aminonitril e, dinitrile and diamine and optionally additional polyamide-forming monomers and/or oligomers with water in a reactor (1) with a vertical longitudinal axis. According to said method, the reaction product is exfiltrated from the sump in the reactor (1) and accumulated ammonia and optionally other accumulated low-molecular compounds and water are drawn off via the head (2) . The invention is characterised in that the reactor (1) comprises at least tw o chambers (4) arranged in a longitudinal direction one above the other, that the chambers (4) are separated from one another by liquid-tight floors (5), that each chamber (4) is connected to the one (4) immediately below by a respective liquid overflow (6) and a liquid product stream is drawn off via the liquid overflow (6) of the lowest chamber (4), that the gas chamber (7) above the liquid level in each chamber (4) is connected to the respective chamber (4) lying immediately above it via one or several conduits (8), whic h open respectively into a gas diffuser (9) comprising orifices (11) for the discharge of gas below the liquid level. The reactor also comprises at least one respective deflector plate (12) positioned vertically around each gas diffuser (9), the upper end of said plate terminating below the liquid level and the lower end terminating above the liquid-tight floor (5) of the chambe r (4), thus sub-dividing each chamber (4) into one or more compartments suppli ed with gas (13) and one or more compartments without gas (14).
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