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公开(公告)号:DE10131788A1
公开(公告)日:2003-01-16
申请号:DE10131788
申请日:2001-07-04
Applicant: BASF AG
Inventor: WOSTBROCK KARL-HEINZ , THIEL JOACHIM , GERBER BERND , KRUEGER HEINZ , STROEFER ECKHARD , KERTH STEFFEN , SACHWEH BERND , RUMPF BERND , WEBER MARKUS
Abstract: The invention relates to a method for producing a highly pure, aqueous hydroxylamine solution by distilling an aqueous solution, devoid of salt, of a hydroxyl ammonium salt in a plate column comprising at least two mechanical plates. Said method is characterised in that packing bodies are arranged between at least two plates of the plate column over the cross-section of said column.
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公开(公告)号:DE10129233A1
公开(公告)日:2003-01-02
申请号:DE10129233
申请日:2001-06-19
Applicant: BASF AG
Inventor: WOELFERT ANDREAS , MUELLER CHRISTIAN , STROEFER ECKHARD
IPC: C07C263/10 , C07C265/14
Abstract: The invention relates to a method for producing isocyanates by reacting primary amines with phosgene, and using isocyanate as the solvent. The inventive method is characterized in that a portion or the entire quantity of the isocyanate used as the solvent is only added to the reaction batch once the amine and the phosgene have been combined.
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公开(公告)号:NO20025379D0
公开(公告)日:2002-11-08
申请号:NO20025379
申请日:2002-11-08
Applicant: BASF AG
Inventor: STROEFER ECKHARD , WOSTBROCK KARL-HEINZ , WEBER MARKUS
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公开(公告)号:AT220386T
公开(公告)日:2002-07-15
申请号:AT98943835
申请日:1998-08-04
Applicant: BASF AG
Inventor: WATZENBERGER OTTO , MAUER PETER , STROEFER ECKHARD , SCHELLING HEINER , SCHNEIDER HANS-MICHAEL
IPC: C01B21/14
Abstract: An aqueous solution of free hydroxylamine is prepared by treating a hydroxylammonium salt with ammonia by the countercurrent method in a stripping column by a process in which hydroxylamine is liberated and at the same time the solution obtained is separated by distillation into an aqueous hydroxylamine solution and a salt fraction. The novel process can be carried out in a simple and gentle manner and on a large scale. The danger of decomposition is minimized owing to the low thermal load, the low concentration of hydroxylamine and the short residence time in the process.
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公开(公告)号:TR200000299T2
公开(公告)日:2001-01-22
申请号:TR200000299
申请日:1998-08-04
Applicant: BASF AG
Inventor: WATZENBERGER OTTO , MAUER PETER , STROEFER ECKHARD , SCHELLING HEINER , SCHNEIDER HANS-MICHAEL
IPC: C01B21/14
Abstract: An aqueous solution of free hydroxylamine is prepared by treating a hydroxylammonium salt with ammonia by the countercurrent method in a stripping column by a process in which hydroxylamine is liberated and at the same time the solution obtained is separated by distillation into an aqueous hydroxylamine solution and a salt fraction. The novel process can be carried out in a simple and gentle manner and on a large scale. The danger of decomposition is minimized owing to the low thermal load, the low concentration of hydroxylamine and the short residence time in the process.
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公开(公告)号:DE19925870A1
公开(公告)日:2000-12-14
申请号:DE19925870
申请日:1999-06-07
Applicant: BASF AG
Inventor: STROEFER ECKHARD , SCHOLL STEPHAN , HASSE HANS
IPC: B01D1/22 , C07B63/00 , C07C29/80 , C07C41/56 , C07C43/303 , C07C45/82 , C07C47/04 , C07C47/058 , C07B61/00
Abstract: A method for reacting a solution containing a mixture of at least two chemicals in chemical equilibrium with other chemical(s) involves: (a) separating the solution into at least two fractions, enriched in the various compounds relative to the equilibrium concentrations; and (b) reacting one fraction with the other reactant(s) before equilibrium is completely restored. A method for reacting a solution containing a mixture of at least two chemicals in chemical equilibrium with other chemical(s) involves: (1) separating the solution into at least two fractions, enriched in the various compounds relative to the equilibrium concentrations; and (2) reacting one fraction with the other reactant(s) before equilibrium is completely restored. Excluded is the reaction of a formaldehyde solution, containing polyoxymethylene glycols and optionally monomeric formaldehyde and/or methylene glycol, with aniline in presence of an acid catalyst.
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公开(公告)号:NO20000551L
公开(公告)日:2000-04-04
申请号:NO20000551
申请日:2000-02-03
Applicant: BASF AG
Inventor: WATZENBERGER OTTO , MAUER PETER , STROEFER ECKHARD , SCHELLING HEINER , SCHNEIDER HANS-MICHAEL
Abstract: An aqueous solution of free hydroxylamine is prepared by treating a hydroxylammonium salt with ammonia by the countercurrent method in a stripping column by a process in which hydroxylamine is liberated and at the same time the solution obtained is separated by distillation into an aqueous hydroxylamine solution and a salt fraction. The novel process can be carried out in a simple and gentle manner and on a large scale. The danger of decomposition is minimized owing to the low thermal load, the low concentration of hydroxylamine and the short residence time in the process.
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公开(公告)号:NO20000551A
公开(公告)日:2000-04-04
申请号:NO20000551
申请日:2000-02-03
Applicant: BASF AG
Inventor: WATZENBERGER OTTO , MAUER PETER , STROEFER ECKHARD , SCHELLING HEINER , SCHNEIDER HANS-MICHAEL
CPC classification number: C01B21/1445
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公开(公告)号:DE19828510A1
公开(公告)日:1999-12-30
申请号:DE19828510
申请日:1998-06-26
Applicant: BASF AG
Inventor: STROEFER ECKHARD , PFEFFINGER JOACHIM
IPC: B01J19/18 , C07C263/10 , C07C265/08 , C07C265/14 , C07C263/20
Abstract: In the simultaneous production of isocyanates (I) by reacting the corresponding amines (II) with phosgene (COCl2), reaction is carried out in a mixer and subsequent dwell reactor, then the reaction mixture is freed from excess COCl2 and hydrogen chloride (HCl) and separated into individual (I) fractions.
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公开(公告)号:AU2006310719B2
公开(公告)日:2011-03-31
申请号:AU2006310719
申请日:2006-06-12
Applicant: BASF AG
Inventor: BLAGOV SERGEJ , HASSE HANS , STROEFER ECKHARD
IPC: C08G65/00
Abstract: Preparing tri-/tetra oxymethylene glycol dimethylether (I) comprises e.g. distilling an aqueous formaldehyde solution and methanol in a reactor to form a reaction mixture containing polyoxy methylene glycol dimethylether (III); distilling the reaction mixture to form a high-boiling fraction (A2) containing e.g. (III); distilling (A2) to form e.g. a low-boiling fraction (A3) having e.g. (I); distilling (A3) to form a high-boiling fraction (A5) having e.g. (I); and distilling (A5) to form an organic phase containing (I). Preparing tri-/tetra oxymethylene glycol dimethylether through the conversion of formaldehyde with methanol and successive distillation of a reaction mixture, comprises: feeding an aqueous formaldehyde solution and methanol in a reactor to form the reaction mixture containing formaldehyde, water, methylene glycol, polyoxymethylene glycol, methanol, hemiformal, methylal and polyoxymethylene glycol dimethylether (III); feeding the reaction mixture into a first distillation column (5) and separating a low-boiling fraction (A1) containing formaldehyde, water, methylene glycol, methanol, methylal and polyoxy methylene glycoldimethylether and a high-boiling fraction (A2) containing formaldehyde, water, methanol, polyoxymethylene glycol, hemiformal and (III); feeding (A2) into a second distillation column (8) and separating a low-boiling fraction (A3) containing formaldehyde, water, methylene glycol, polyoxymethylene glycol, methanol, hemiformal, di-chloroethylene and (I) and a high-boiling containing polyoxymethylene glycol, high-boiling hemiformal and high-boiling polyoxymethylene glycol dimethylether; feeding (A3) and optionally feed-back stream containing formaldehyde, water, methylene glycol and polyoxymethylene glycol into a third distillation column (13) and separating a high volatile fraction (A4) containing formaldehyde, water, methanol, polyoxymethylene glycol, hemiformal and dioxymethylene glycol dimethylether and a high-boiling fraction (A5) containing formaldehyde, water, methylene glycol, polyoxymethylene glycol and (I); feeding (A5) in to a phase separator and separating an aqueous phase containing formaldehyde, water, methylene glycol and polyoxymethyleneglycol and an organic phase containing (I); feeding the organic phase into a fourth distillation column (18) and separating a low-boiling fraction (A6) containing formaldehyde, water, methylene glycol and polyoxymethylene glycol and a high-boiling fraction containing (I); and optionally feeding the aqueous phase in a fifth distillation column (24) and separating a low-boiling fraction (A7) containing formaldehyde, water, methylene glycol and polyoxymethylene glycol and a high-boiling fraction containing water.
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