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公开(公告)号:DE4418488A1
公开(公告)日:1995-11-30
申请号:DE4418488
申请日:1994-05-27
Applicant: BASF AG
Inventor: KAIBEL GERD DR
Abstract: The distillative sepn. of material mixts. into their pure components comprises using a distn. column contg. complete or part packing of ordered or unordered sepn. elements. Between a boiler and a condenser, rising steam and falling fluid come into intimate contact, and through the resulting mass transfer the lower boiling components are obtd. in the condenser and the higher boiling ones in the column reboiler. In the column, an uneven distribution of the liq. scrubbing density is aimed for across the column cross section. Also claimed is a device to carry out the above process comprising a distn. column with liq. collectors and redistribution devices. According to the desired liq. scrubbing density in the core as well as the wall region of the column, the arrangement of the outflow openings and/or their dia. are optimised.
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公开(公告)号:ES2062115T3
公开(公告)日:1994-12-16
申请号:ES90101132
申请日:1990-01-20
Applicant: BASF AG
Inventor: KAIBEL GERD DR , SCHLOEMER KARL DR , MAYER HANS-HORST
Abstract: Process for the separation by distillation of small quantities of a middle-boiling fraction from a liquid mixture by means of a distillation column (main column), comprising a rectification and a stripping component, where the liquid mixture contains relatively large amounts of higher- and lower-boiling constituents, and the rectification component being connected to the upper end and the stripping component to the lower end of a second distillation column (side column), and the middle-boiling fraction being removed in vapour or liquid form from its middle region, the concentration of the middle-boiling fraction in the liquid mixture being less than 2%, preferably less than 0.1%, and the amount of vapour introduced into the side column at its lower end from the main column being 1 to 20%, preferably 3 to 10%, relative to the amount of vapour in the main column at the relevant point.
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公开(公告)号:AT66447T
公开(公告)日:1991-09-15
申请号:AT88104604
申请日:1988-03-23
Applicant: BASF AG
Inventor: KAIBEL GERD DR , HEFNER WERNER DR , KELLER PETER DR , DREWITZ WERNER
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公开(公告)号:DE3902006A1
公开(公告)日:1990-07-26
申请号:DE3902006
申请日:1989-01-25
Applicant: BASF AG
Inventor: KAIBEL GERD DR , SCHLOEMER KARL DR , MAYER HANS-HORST
Abstract: Process for the separation by distillation of small quantities of a middle-boiling fraction from a liquid mixture by means of a distillation column (main column), comprising a rectification and a stripping component, where the liquid mixture contains relatively large amounts of higher- and lower-boiling constituents, and the rectification component being connected to the upper end and the stripping component to the lower end of a second distillation column (side column), and the middle-boiling fraction being removed in vapour or liquid form from its middle region, the concentration of the middle-boiling fraction in the liquid mixture being less than 2%, preferably less than 0.1%, and the amount of vapour introduced into the side column at its lower end from the main column being 1 to 20%, preferably 3 to 10%, relative to the amount of vapour in the main column at the relevant point.
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公开(公告)号:ES2202507T5
公开(公告)日:2008-05-01
申请号:ES97104966
申请日:1997-03-24
Applicant: BASF AG
Inventor: KAIBEL GERD DR , BROCKER FRANZ-JOSEF DR , STROEZEL MANFRED
IPC: B01F5/06 , B01J19/24 , B01J8/00 , B01J8/06 , B01J8/18 , B01J8/20 , B01J8/22 , B01J8/34 , C07C45/62
Abstract: LA PRESENTE INVENCION ESTA RELACIONADA CON UN METODO PARA REALIZAR REACCIONES CATALITICAS EN UN REACTOR QUE CONTIENE UNA FASE LIQUIDA EN LA QUE ESTA SUSPENDIDO COMO MINIMO UN CATALIZADOR, Y QUE OPCIONALMENTE PUEDE CONTENER UNA FASE GASEOSA. LA FASE LIQUIDA Y, SI ESTA PRESENTE, TAMBIEN LA FASE GASEOSA SON ENVIADAS COMO MINIMO PARCIALMENTE A TRAVES DE UN DISPOSITIVO CON ABERTURAS O CANALES AL REACTOR, CUYO DIAMETRO HIDRAULICO ES DE 0,5 A 20 MM, PREFERENTEMENTE DE 1 A 10 MM, Y OPTIMAMENTE DE 1 A 3 MM.
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公开(公告)号:AT253542T
公开(公告)日:2003-11-15
申请号:AT01120387
申请日:2001-08-25
Applicant: BASF AG
Inventor: THERRE JOERG DR , KAIBEL GERD DR , AQUILA WERNER DR , WEGNER GUENTER DR , FUCHS HARTWIG
IPC: C07C41/50 , C07B61/00 , C07C41/56 , C07C41/58 , C07C43/303
Abstract: Preparation of acetals by reaction of 1 mol. of an unsaturated aldehyde with 1 mol. of an unsaturated alcohol in presence of an acid as catalyst and with separation of the water of reaction is effected by partly reacting the reactants in a column, concentrating the obtained acetal in ≥ 2 sequential evaporation steps and then recycling the recovered reactants to the reaction column. Preparation of acetals (I) by reaction of 1 mol. of an unsaturated aldehyde (II) with 1 mol. of an unsaturated alcohol (III) in presence of an acid as catalyst and with separation of the water of reaction is effected by partly reacting the reactants in a column, concentrating the obtained acetal in ≥ 2 sequential evaporation steps and then recycling the recovered reactants to the reaction column. R - R = H or optionally substituted 1-6C alkyl; and R = H, an optionally mono- or poly-unsaturated, optionally substituted 1-12C alkyl or an optionally substituted 3-12-membered optionally mono- or poly-unsaturated carbon ring.
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公开(公告)号:AT243072T
公开(公告)日:2003-07-15
申请号:AT97104966
申请日:1997-03-24
Applicant: BASF AG
Inventor: KAIBEL GERD DR , BROECKER FRANZ-JOSEF DR , STROEZEL MANFRED
IPC: B01F5/06 , B01J8/00 , B01J8/06 , B01J8/18 , B01J8/20 , B01J8/22 , B01J8/34 , B01J19/24 , C07C45/62
Abstract: In carrying out reactions in a reactor containing a liquid phase in which a catalyst is suspended, and where a gaseous phase may be present, the liquid and gas phases pass, at least partly, through a device having openings or passages whose hydraulic diameter is 0.5-20 (1-3) mm. Also claimed is the reactor including a device having openings or passages in it built so that liquid or gas flow through it during the reaction.
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公开(公告)号:ES2183038T3
公开(公告)日:2003-03-16
申请号:ES97106627
申请日:1997-04-22
Applicant: BASF AG
Inventor: KAIBEL GERD DR , STROEZEL MANFRED , RHEUDE UDO DR
Abstract: A partitioned column for separating a multi-component mixture into three or more fractions comprises at least one removable partition wall. Also claimed is a process for separating a multi-component mixture into three or more fractions using the above column.
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公开(公告)号:AT232193T
公开(公告)日:2003-02-15
申请号:AT99118458
申请日:1999-09-17
Applicant: BASF AG
Inventor: THERRE JOERG DR , KAIBEL GERD DR , AQUILA WERNER DR , WEGNER GUENTER DR , FUCHS HARTWIG
IPC: B01J27/16 , C07B61/00 , C07C41/28 , C07C43/15 , C07C45/37 , C07C45/51 , C07C45/54 , C07C45/67 , C07C47/21 , C07C49/203
Abstract: Preparation of citral (I) comprises thermal decomposition of 3-methyl-2-buten-1-al-diprenylacetal and rearrangement of obtained intermediates cis/trans-prenyl-(methyl-butadienyl)-ether (IV) and 2,4,4-trimethyl-3-formyl-1,5-hexadiene (V). (IV) and (V) are continuously distilled off and converted into (I) before or after removal of by-product prenol. Preparation of 3,7-dimethyl-2,6-octadien-1-al (citral) of formula (I) comprises: (1) thermal decomposition of 3-methyl-2-buten-1-al-diprenylacetal of formula (II) optionally in the presence of an acid catalyst to split off 3-methyl-buten-1-ol (prenol) of formula (III) and form cis/trans-prenyl-(methyl-butadienyl)-ether of formula (IV); (2) Claisen rearrangement of (IV) to give 2,4,4-trimethyl-3-formyl-1,5-hexadiene of formula (V); and (3) Cope rearrangement of (V) to form (I). The transitionally formed (IV) and (V) and the desired citral as well as the prenol (III) are continuously distilled out of the reaction mixture and (IV) and (V), before or after distillative separation of (III) and optional by-products, are subjected to rearrangement to form (I) at 100-200 degrees C.
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公开(公告)号:DE19611976A1
公开(公告)日:1997-10-02
申请号:DE19611976
申请日:1996-03-26
Applicant: BASF AG
Inventor: KAIBEL GERD DR , BROECKER FRANZ JOSEF DR , STROEZEL MANFRED
IPC: B01F5/06 , B01J8/00 , B01J8/06 , B01J8/18 , B01J8/20 , B01J8/22 , B01J8/34 , B01J19/24 , C07C45/62
Abstract: In carrying out reactions in a reactor containing a liquid phase in which a catalyst is suspended, and where a gaseous phase may be present, the liquid and gas phases pass, at least partly, through a device having openings or passages whose hydraulic diameter is 0.5-20 (1-3) mm. Also claimed is the reactor including a device having openings or passages in it built so that liquid or gas flow through it during the reaction.
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