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公开(公告)号:DE502005011240D1
公开(公告)日:2011-05-26
申请号:DE502005011240
申请日:2005-01-27
Applicant: BASF SE
Inventor: JUNGKAMP TIM , BAUMANN ROBERT , BARTSCH MICHAEL , HADERLEIN GERD , LUYKEN HERMANN , SCHEIDEL JENS
IPC: C07C253/10 , C07C255/07
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公开(公告)号:DE50313458D1
公开(公告)日:2011-03-17
申请号:DE50313458
申请日:2003-11-11
Applicant: BASF SE
Inventor: FISCHER ROLF-HARTMUTH , LUYKEN HERMANN , ANSMANN ANDREAS , BASLER PETER , BENISCH CHRISTOPH , MAIXNER STEFAN , MELDER JOHANN-PETER
IPC: C07D201/16 , C07D201/08
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公开(公告)号:AT501114T
公开(公告)日:2011-03-15
申请号:AT05707030
申请日:2005-01-27
Applicant: BASF SE
Inventor: SCHEIDEL JENS , JUNGKAMP TIM , BARTSCH MICHAEL , HADERLEIN GERD , BAUMANN ROBERT , LUYKEN HERMANN
IPC: C07C253/10 , C07C255/07
Abstract: A process is described for preparing 3-pentenenitrile by hydrocyanating 1,3-butadiene, wherein 1,3-butadiene is reacted with hydrogen cyanide in the presence of at least one catalyst and the stream resulting therefrom is purified distillatively, the bottom temperature during the distillation not exceeding 140° C.
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公开(公告)号:MX2010005157A
公开(公告)日:2010-11-26
申请号:MX2010005157
申请日:2008-11-10
Applicant: BASF SE
Inventor: LUYKEN HERMANN , PFAB PETER , SCHNEIDER THOMAS , DECKERS ANDREAS , BOEHLING RALF , ACHHAMMER GUENTHER , SCHUBERT KLAUS , KRAUT MANFRED
IPC: C01C3/02
Abstract: La invención se refiere a un método para la producción de ácido cianhídrico, que consiste en la disposición de formamida gaseosa por evaporación de la formamida líquida en un evaporador (paso i)) y la deshidratación catalítica de la formamida gaseosa (paso ii)), y un dispositivo para llevar a cabo el método de acuerdo con la invención, el dispositivo consiste en al menos un microevaporador y un reactor tubular, y el uso de un microevaporador para evaporar formamida en un método para la producción de ácido cianhídrico a partir de formamida.
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公开(公告)号:DE502005010038D1
公开(公告)日:2010-09-16
申请号:DE502005010038
申请日:2005-01-27
Applicant: BASF SE
Inventor: SCHEIDEL JENS , JUNGKAMP TIM , BARTSCH MICHAEL , HADERLEIN GERD , BAUMANN ROBERT , LUYKEN HERMANN
IPC: C07C253/10 , C07C253/34 , C07C255/07
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公开(公告)号:CL2008003380A1
公开(公告)日:2010-01-11
申请号:CL2008003380
申请日:2008-11-13
Applicant: BASF SE
Inventor: SCHNEIDER THOMAS , DECKERS ANDREAS , BOHLING RALF , ACHHAMMER GUNTHER , LUYKEN HERMANN , PFAB PETER
Abstract: Procedimiento de preparación de HCN por deshidratación catalítica de formamida gaseosa en reactor tubular formado por al menos un canal de reacción, de superficie interna de un material que comprende igual o mayor a 50% peso de hierro, donde dicho canal presenta diámetro hidráulico medio de 0,5 a 6 mm; reactor y su uso.
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公开(公告)号:DE50114970D1
公开(公告)日:2009-08-20
申请号:DE50114970
申请日:2001-04-30
Applicant: BASF SE
Inventor: OHLBACH FRANK , ANSMANN ANDREAS , BASSLER PETER , FISCHER ROLF-HARTMUTH , LUYKEN HERMANN , MAIXNER STEFAN , MELDER JOHANN-PETER
IPC: C07D201/08 , C07D223/10 , C07B61/00 , C07D207/263 , C07D211/76 , C07D225/02
Abstract: The invention relates to a method for producing cyclic lactams of the formula (II), wherein n and m may each represent 0, 1, 2, 3, 4, 5, 6, 7, 8 and 9 and the sum of n + m is at least 3, preferably at least 4, R and R represent C1-C6 alkyl, C5-C7 cycloalkyl or C6-C12 aryl groups, by reacting a compound of the formula (I), wherein R , R , m and n have the meaning indicated above, and R represents nitrile groups, carboxylic acid amide groups and carboxylic acid groups, with water vapor in the gaseous phase. The inventive method is further characterized in that a) the compound (I) is reacted with water vapor in the gaseous phase, adding an organic diluent (III) before or after the reaction, which diluent has a miscibility gap under certain quantitative, pressure and temperature conditions, said reaction resulting in a mixture (IV) that contains a lactam (II), b) adjusting the mixture (IV) before or after the removal of ammonia to quantitative, pressure and temperature conditions under which the diluent (III) and water are present in a liquid form and have a miscibility gap, and obtaining a two-phase system consisting of a phase (V) that has a higher proportion of diluent (III) than water, and a phase (VI) that has a higher proportion of water than diluent (III), c) separating phase (V) from phase (VI) and, d) removing from phase (V) the diluent (III) and optionally by-products selected from the group of the low-boilers, high-boilers and unreacted compound (I), and obtaining a lactam (II).
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公开(公告)号:PL1817108T3
公开(公告)日:2008-11-28
申请号:PL05798767
申请日:2005-10-12
Applicant: BASF SE
Inventor: DECKERT PETRA , BASSLER PETER , BARTSCH MICHAEL , HADERLEIN GERD , LUYKEN HERMANN , SCHEIDEL JENS , PFAB PETER , AECHTNER TOBIAS , SIEGEL WOLFGANG
IPC: B01J31/40 , B01D11/04 , B01J31/18 , B01J31/24 , B01J38/56 , C07C253/10 , C07C253/32
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19.
公开(公告)号:ES2306233T3
公开(公告)日:2008-11-01
申请号:ES05798767
申请日:2005-10-12
Applicant: BASF SE
Inventor: DECKERT PETRA , BASSLER PETER , BARTSCH MICHAEL , HADERLEIN GERD , LUYKEN HERMANN , SCHEIDEL JENS
IPC: B01J31/40 , B01D11/04 , B01J31/18 , B01J31/24 , B01J38/56 , C07C253/10 , C07C253/32
Abstract: Procedimiento para la separación por extracción de catalizadores disueltos, homogéneos, a partir de una descarga de la reacción de una hidrocianuración de mononitrilos insaturados para dar dinitrilos, mediante extracción con ayuda de un hidrocarburo K, caracterizado porque a) se concentra por evaporación la descarga de la reacción como paso previo a la etapa b) mediante destilación a presiones comprendidas entre 0,1 y 5.000 mbares y a temperaturas comprendidas entre 10 y 150ºC, b) se aporta un hidrocarburo K a la descarga de la reacción, concentrada por evaporación, con lo que se obtiene una corriente I, y c) se alimenta la corriente I, sin separación previa de las fases líquidas, en un dispositivo de extracción y se extrae a una temperatura T con el hidrocarburo K, obteniéndose una corriente II que contiene el hidrocarburo K enriquecido con el catalizador, y una corriente III pobre en catalizador.
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公开(公告)号:DE502005004577D1
公开(公告)日:2008-08-14
申请号:DE502005004577
申请日:2005-01-27
Applicant: BASF SE
Inventor: JUNGKAMP TIM , BAUMANN ROBERT , BARTSCH MICHAEL , HADERLEIN GERD , LUYKEN HERMANN , SCHEIDEL JENS
IPC: C07C253/10 , C07C255/04
Abstract: An adiponitrile/methylglutaronitrile preparation process includes distilling a reaction stream to obtain stream 3 depleted in pentenenitriles (bottom product) and stream 4 enriched in pentenenitriles (top product); extracting stream 3 obtaining stream 6 enriched with extractant (top product) and stream 7 depleted in extractant (bottom product); distilling stream 6 obtaining stream 8 comprising the catalyst (bottom product) and stream 9 comprising the extractant (top product); distilling stream 7 obtaining stream 10 (bottom product) and stream 11 comprising the extractant (top product); distilling stream 10 obtaining stream 12 comprising catalyst degradation products, at least one promotor, adiponitrile and methylglutaronitrile (bottom product) and stream 13 comprising pentenenitriles (top product); distilling stream 12 obtaining stream 14 comprising catalyst degradation products and the promotor(s) (bottom product) and stream 15 comprising adiponitrile and methylglutaronitrile (top product); distilling stream 15 obtaining stream 16 comprising adiponitrile (bottom product) and stream 17 comprising methylglutaronitrile (top product).
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