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公开(公告)号:DE19704616A1
公开(公告)日:1998-08-13
申请号:DE19704616
申请日:1997-02-07
Applicant: BASF AG
Inventor: LUYKEN HERMANN , REHFINGER ALWIN DR , BASLER PETER DR , VOIT GUIDO DR , FISCHER ROLF DR , MERGER MARTIN DR , RUST HARALD
IPC: C07C209/84 , C07C211/12 , C07C211/36
Abstract: The invention relates to a method for separating 2-aminomethylcyclopentylamine from a mixture containing hexamethylene diamine and 2-aminomethylcyclopentyl-amine, characterized in that separation by distillation occurs at a pressure of 1-3,000 mbars.
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62.
公开(公告)号:CA2279172A1
公开(公告)日:1998-08-13
申请号:CA2279172
申请日:1998-01-17
Applicant: BASF AG
Inventor: LUYKEN HERMANN , BASSLER PETER , RUST HARALD , REHFINGER ALWIN
IPC: C07C255/24 , C07C253/34
Abstract: The invention relates to a method for separating 6-aminocapronitrile from mixtures (I) containing 6-aminocapronitrile and an imine (II) by distillation. Said method is characterized in that distillation occurs in the presence of carbon dioxide.
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公开(公告)号:CA2265436A1
公开(公告)日:1998-03-19
申请号:CA2265436
申请日:1997-08-28
Applicant: BASF AG
Inventor: BASSLER PETER , RUST HARALD , FISCHER ROLF , VOIT GUIDO , LUYKEN HERMANN , REHFINGER ALWIN , MERGER MARTIN
IPC: C07C209/86 , C07C211/12 , C07C211/36
Abstract: Process for the separation of 2-aminomethylcyclopentylamine from a mixture containing hexamethyldiamine and 2-aminomethylcyclopentylamine, characterized by the fact that the separation is carried out by means of distillation at a pressure of 1-300 mbars.
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公开(公告)号:NO980869L
公开(公告)日:1998-02-27
申请号:NO980869
申请日:1998-02-27
Applicant: BASF AG
Inventor: ARON MAIK , RUST HARALD
Abstract: PCT No. PCT/EP96/03762 Sec. 371 Date Feb. 17, 1998 Sec. 102(e) Date Feb. 17, 1998 PCT Filed Aug. 26, 1995 PCT Pub. No. WO97/08120 PCT Pub. Date Mar. 6, 1997Butanol and dibutyl ether are separated from a mixture containing water, dibutyl ether and n-butanol, 2-butanol and/or isobutanol by a process in which a) the mixture is introduced into a first distillation column, essentially butanol is separated off at the bottom of this distillation column and the mixture taken off at the top of the distillation column b) is introduced into a second distillation column and essentially dibutyl ether is separated off at the bottom of this second distillation column and the mixture formed at the top of the second distillation column is removed, c) the second distillation column being operated at a higher pressure than the first distillation column and at least one of the two mixtures taken off via the top of the distillation columns being subjected to phase separation, only the organic phase separated off being fed to the second distillation column in the case of phase separation downstream of the first distillation column, and separation into an aqueous and an organic phase also being effected in the case of phase separation downstream of the second distillation column, a part stream being recycled from the top or rectification section of the second distillation column to the first distillation column.
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公开(公告)号:ES2107886T3
公开(公告)日:1997-12-01
申请号:ES95112004
申请日:1995-07-31
Applicant: BASF AG
Inventor: RUHL THOMAS DR , HEIDER MARC DR , HENKELMANN JOCHEM DR , RAHN RALF-THOMAS DR , RUST HARALD
Abstract: Recovery of pure vinyl formate (I) by distn. to separate by-prodn. from synthesis is carried out in two stages, HCOOH and water being sepd. in stage one and CH3CHO in stage two.
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公开(公告)号:CA2248004A1
公开(公告)日:1997-09-04
申请号:CA2248004
申请日:1997-02-28
Applicant: BASF AG
Inventor: RUST HARALD , BREITSCHEIDEL BORIS , STEIN FRANK , FISCHER ROLF , PINKOS ROLF , BAUR KARL GERHARD
IPC: C07D313/04 , C07C27/12 , C07C29/149 , C07C29/80 , C07C29/88 , C07C31/20 , C07C31/27 , C07C51/31 , C07D315/00
Abstract: The invention relates to a process for preparing 1,6 hexane diol and .epsilon.caprolacton from a carboxylic acid mixture containing adipic acid, 6-hydroxy caproic acid and, in small quantities, 1,4 cyclohexane diols. Said mixture is obtained as a by-product of the oxidation of cyclohexane into cyclohexanone/ cyclohexanol with oxygen or gases containing oxygen, by water extraction of the reaction mixture. Said process involves esterification and hydrogenation of a partial stream into hexane diol and cyclization of 6-hydroxy caproic acid esters into caprolacton. According to this process: (a) the monocarboxylic acids and the dicarboxylic acids contained in the aqueous reaction mixture are reacted with a low-molecular alcohol to form the corresponding carboxylic acid esters; (b) the excess alcohol, water and low-boiling agents of the resultant esterification mixture are released in a first distillation stage; (c) separating into a ester fraction substantially free of 1,4 cyclohexane diols, and a fraction containing at least the greater part of the 1,4 cyclohexane diols is carried out from the bottom product in a second distillation stage; (d) at least part of a stream substantially containing 6-hydroxy caproic acid ester is separated from the ester fraction in a third distillation stage; (e) the ester fraction from (d), from which 6-hydroxy caproic acid ester was at least partially removed, is hydrogenated catalytically and 1,6 hexane diol is extracted by distilling the hydrogenated product in a known manner; and (f) the stream substantially containing 6-hydroxy caproic acid ester is heated to temperatures above 200 ~C at reduced pressure, thereby causing cyclization of 6-hydroxy caproic acid ester to form caprolacton, and pure .epsilon.caprolacton is recovered from the cyclization product by distillation.
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公开(公告)号:CA2227280A1
公开(公告)日:1997-03-06
申请号:CA2227280
申请日:1996-08-26
Applicant: BASF AG
Inventor: RUST HARALD , ARON MAIK
Abstract: A process for separating butanol and dibutyl ether from a mixture containing water, dibutyl ether and n-butanol, 2-butanol and/or iso-butanol, in which: a) the mixture is introduced into a first distillation column, butanol is essentially separated in its sump and the mixture drawn from the top of the distillation column is b) introduced into a second distillation column and essentially dibutyl ether is separated off in its sump and the mixture form at its top is drawn off, whereby c) the second distillation column is operated at a higher pressure than the first and at least one of the two mixtures drawn off from the head of the distillation columns is taken to a phase separation, where in the case of phase separation behind the first distillation column, only the separated organic phase is taken to the second column and, in the case of phase separation behind the second column, the phases are separated into an aqueous and an organic phase and a partial flow from the head or concentration section of the second distillation column is fed back into the first column.
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公开(公告)号:ES2055837T3
公开(公告)日:1994-09-01
申请号:ES90115637
申请日:1990-08-16
Applicant: BASF AG
Inventor: STECK WERNER DR , RUST HARALD , LERMER HELMUT DR , FRITZ NAEUMANN DR
IPC: C07C253/34 , C07C255/50
Abstract: A process for the separation of ortho-, meta- and para-tolunitrile from ternary mixtures of isomers entails removing ortho-tolunitrile from these mixtures by distillation under pressures of from 102 and 105 Pa and with a reflux ratio of from 1:1 to 200:1, and distilling the remaining binary mixture of meta- and para-tolunitrile to concentrate to more than 75 mol-% para-tolunitrile, and freezing out the paratolunitrile at below 26 DEG C., and a process for the preparation of suitable ternary mixtures of isomers entails isomerization of pure ortho-, meta- or para-tolunitrile or mixtures thereof at from 380 DEG to 580 DEG C. on zeolite catalysts.
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公开(公告)号:DE502004002451D1
公开(公告)日:2007-02-08
申请号:DE502004002451
申请日:2004-02-26
Applicant: BASF AG
Inventor: FISCHER ROLF-HARTMUTH , GALL MARTIN , HUBER-DIRR SYLVIA , LIANG SHELUE , NOEBEL THOMAS , RUST HARALD , STEIN FRANK
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公开(公告)号:AT330923T
公开(公告)日:2006-07-15
申请号:AT00985231
申请日:2000-12-21
Applicant: BASF AG
Inventor: DERNBACH MATTHIAS , KRATZ DETLEF , STAMMER ACHIM , RUST HARALD , SCHULZ GERHARD
IPC: C07B61/00 , C07C29/80 , C07C31/22 , C07C29/141
Abstract: A process is disclosed for the purification, by distillation, of trimethylolpropane originating from the hydrogenation of 2,2-dimethylolbutanal, said process including the following steps:(a) reaction of n-butyraldehyde with formaldehyde in the presence of catalytic amounts of a tertiary amine, and hydrogenation of the resulting mixture to give a mixture containing trimethylolpropane;(b) separation of water, methanol, trialkylamine and/or trialkylammonium formate by distillation;(c) heating of the residue obtained in (b) under reduced pressure to a temperature at which TMP is volatile and compounds boiling above TMP are cleaved, in order to separate off, by distillation, TMP and compounds more volatile than TMP;(d) distillation of the distillate obtained in (c) in order to separate off the more volatile compounds and recover pure TMP; and(e) optional distillation of the TMP obtained in (d) in order to recover TMP with a low APHA color index.A process is also disclosed in which trialkylammonium formate is distilled under mild conditions from crude mixtures of polyhydric alcohols, predominantly trimethylolpropane.
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