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公开(公告)号:DE10328713A1
公开(公告)日:2005-01-20
申请号:DE10328713
申请日:2003-06-25
Applicant: BASF AG
Inventor: STUEER WOLFRAM , SCHEIDEL JENS , VOS HARTWIG , BASLER PETER , ROEPER MICHAEL
Abstract: A process for separating a mixture comprising a) a monoolefinically unsaturated compound which is obtainable by adding two terminal olefins which bear the functional groups required to prepare the monoolefinically unsaturated compound containing at least two functional groups, or a saturated compound obtained by hydrogenating such a compound, b) a compound which is obtainable by adding more than two of the terminal olefins mentioned in a) or a compound obtained by hydrogenating such a compound, and c) a compound which contains a transition metal, is homogeneous with respect to the mixture and is suitable as a catalyst for preparing a monoolefinically unsaturated compound by adding two terminal olefins which bear the functional groups required to prepare the monoolefinically unsaturated compound containing at least two functional groups, by means of a semipermeable membrane to obtain a permeate and a retentate in such a way that the weight ratio of component b) to component c) in the mixture fed to the semipermeable membrane is smaller than in the retentate.
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公开(公告)号:DE10320635A1
公开(公告)日:2004-11-18
申请号:DE10320635
申请日:2003-05-08
Applicant: BASF AG
Inventor: MUELLER ULRICH , KRUG GEORG , RUDOLF PETER , TELES JOAQUIM HENRIQUE , GOEBBEL HANS-GEORG , BASLER PETER
IPC: C07D301/12 , B01J29/70
Abstract: A method for the production of propylene oxide (PO) by reacting propene with a hydroperoxide in a nitrile-containing solvent in presence of a porous oxide-containing catalyst, involves using a zeolite catalyst with an X-ray crystal structure of the MWW type. An independent claim is also included for formed catalyst bodies containing the above type of zeolite.
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公开(公告)号:DE10317929A1
公开(公告)日:2004-11-11
申请号:DE10317929
申请日:2003-04-17
Applicant: BASF AG
Inventor: BARTSCH MICHAEL , BAUMANN ROBERT , HADERLEIN GERD , FLORES MIGUEL , JUNGKAMP TIM , LUYKEN HERMANN , SCHEIDEL JENS , SIEGEL WOLFGANG , KUNSMANN-KEITEL DAGMAR PASCALE , BASLER PETER
Abstract: A process for dewatering hydrocyanic acid by distillation, which includes distilling crude hydrocyanic acid containing from 50 to 99.9% by weight of HCN, from 0.1 to 40% by weight of water, from 0 to 15% by weight of carbon oxides and optionally from 0.01 to 1% by weight of an involatile stabilizer, at a pressure of from 1 bar to 2.5 bar, a bottom temperature of from 100° C. to 130° C. and a top temperature of from 25° C. to 54° C., in the absence of a volatile stabilizer, in a distillation column to obtain a top draw stream containing purified, anhydrous hydrocyanic acid and carbon oxides and a bottom draw stream including water and, optionally, the involatile stabilizer.
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公开(公告)号:DE10253094A1
公开(公告)日:2004-05-27
申请号:DE10253094
申请日:2002-11-13
Applicant: BASF AG
Inventor: LUYKEN HERMANN , ANSMANN ANDREAS , BENISCH CHRISTOPH , BASLER PETER , FISCHER ROLF-HARTMUTH , MAIXNER STEFAN , MELDER JOHANN-PETER
IPC: C07D201/16 , C07D223/10
Abstract: A process for the purification of crude caprolactam, prepared by reaction of a mixture comprising 6-aminocapronitrile and water, comprises a three stage distillation process with feeding of the crude caprolactam and an inorganic acid having a b. pt. above the b. pt. of the caprolactam to a first distillation column. A process for the purification of crude caprolactam, prepared by reaction of a mixture comprising 6-aminocapronitrile and water in the presence of a catalyst to form a mixture comprising caprolactam, ammonia, water and high and low b. pt. byproducts followed by removal of ammonia to yield a mixture of caprolactam, water and high and low b. pt. byproducts followed by at least partial removal of water to yield a crude caprolactam containing caprolactam and high and low b. pt. byproducts, comprises: (a) feeding of the crude caprolactam and an inorganic acid having a b. pt. above the b. pt. of the caprolactam to a first distillation column; (b) distillation of the crude caprolactam and inorganic acid to form a sump stream and an overhead stream; (c) feeding of the overhead stream to a second distillation column; (d) distillation of the stream to form a sump stream and overhead stream; (e) feeding of the overhead stream to a third distillation column; (f) distillation of the overhead stream to form a sump stream and purified caprolactam in the overhead stream; and (g) feeding of the sump stream to the first distillation column.
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公开(公告)号:DE10249377A1
公开(公告)日:2004-05-06
申请号:DE10249377
申请日:2002-10-23
Applicant: BASF AG
Inventor: GOEBBEL HANS-GEORG , BASLER PETER , TELES JOAQUIM HENRIQUE , RUDOLF PETER , KRUG GEORG , HARDER WOLFGANG
IPC: B01J8/20 , B01J19/24 , C07D301/12 , C07B41/00
Abstract: Continuous process for the epoxidation of olefins by means of hydroperoxide, in which the epoxidation is carried out in a reactor in which at least one catalyst suspended in a liquid phase is present, wherein the liquid phase is passed through a device which has openings or channels and is installed in the reactor and the epoxide-containing liquid is separated off by means of crossflow filtration so that the suspended catalyst is retained in the reaction system.
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公开(公告)号:ZA200300103B
公开(公告)日:2004-02-25
申请号:ZA200300103
申请日:2003-01-06
Applicant: BASF AG
Inventor: BASLER PETER , REHFINGER ALWIN , RIEBER NORBERT , RUDOLF PETER , HENRIQUE TELES JOAQUIM , WENZEL ANNE
IPC: C07D301/12 , C07D301/32 , C07D
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公开(公告)号:DE10233385A1
公开(公告)日:2004-02-12
申请号:DE10233385
申请日:2002-07-23
Applicant: BASF AG
Inventor: BASLER PETER , GOEBBEL HANS-GEORG , TELES JOAQUIM HENRIQUE , RUDOLF PETER
IPC: B01D3/14 , C07C29/10 , C07D301/12 , C07C31/20
Abstract: An apparatus for carrying out a continuous process for preparing propylene glycols.
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公开(公告)号:DE10144891A1
公开(公告)日:2003-03-27
申请号:DE10144891
申请日:2001-09-12
Applicant: BASF AG
Inventor: KLEIN OLIVER , NEGELE ANTON , RUPPEL WILHELM , VOGT VOLKER , SCHNEIDER THOMAS , ACHHAMMER GUENTHER , RESCH PETER , SIEGEL WOLFGANG , BASLER PETER , MENIG HELMUTH
Abstract: Production of hydrogen cyanide and water comprises contacting gaseous formamide with a catalyst at 350-800 deg C in a flow-type reactor with electric resistance heating. An Independent claim is also included for the apparatus for carrying out the above process, comprising either: (a) a flow reactor containing one or more catalyst-coated heating elements that can be heated by means of a voltage source; or (b) one or more flow tubes that can be heated by means of a voltage source and contain a bed of catalyst.
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公开(公告)号:DE10032885A1
公开(公告)日:2002-01-17
申请号:DE10032885
申请日:2000-07-06
Applicant: BASF AG
Inventor: TELES JOAQUIM HENRIQUE , REHFINGER ALWIN , BASLER PETER , WENZEL ANNE , RIEBER NORBERT , RUDOLF PETER
IPC: C07D301/12 , C07D301/32 , C07D303/04
Abstract: The invention relates to a method for the production of propylene oxide in the presence of methanol, during which propylene oxide is separated off from a mixture, comprising propylene oxide and methanol and the resulting mixture comprising methanol is worked up. The invention is characterised in that on working up, methanol is separated from a mixture containing methanol and methyl formate.
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公开(公告)号:DE19831889A1
公开(公告)日:2000-01-27
申请号:DE19831889
申请日:1998-07-17
Applicant: BASF AG
Inventor: FISCHER ROLF , BASLER PETER , LUYKEN HERMANN , OHLBACH FRANK , MELDER JOHANN-PETER , MERGER MARTIN , ANSMANN ANDREAS , REHFINGER ALWIN , VOIT GUIDO
IPC: C07C209/48 , C07C211/12 , C07C209/82
Abstract: The production of hexamethylenediamine (HDA) from adiponitrile (ADN) involves hydrogenation in ammonia with an iron-based catalyst, followed by removal of ammonia, separation of HDA, separation of 6-aminocapronitrile (ACN) and ADN from high-boilers and returning ACN and/or ADN to the hydrogenation stage. A process for the catalytic hydrogenation of adiponitrile (ADN) to hexamethylenediamine (HDA) comprises: (a) hydrogenation of ADN at 70-220 deg C and 100-400 bar in presence of a catalyst based on elementary iron as the active component and with ammonia as solvent, to give a mixture containing ADN, 6-aminocapronitrile (ACN ), HDA and high-boiling products, until the total concentration of ACN and ADN is 1-50 wt.% based on the ammonia-free hydrogenation mixture, (b) removing ammonia, (c) separating HDA, (d) separating ACN and ADN (individually or together) from the high-boilers and (e) recycling ACN and/or ADN to stage (a).
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