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公开(公告)号:DE50307562D1
公开(公告)日:2007-08-09
申请号:DE50307562
申请日:2003-02-28
Applicant: BASF AG
Inventor: FISCHER ROLF-HARTMUTH , ROESCH MARKUS , BOTTKE NILS , WECK ALEXANDER , WINDECKER GUNTHER , HESSE MICHAEL , BORCHERT HOLGER , SCHLITTER STEPHAN
IPC: C07D207/26 , B01J23/72 , B01J23/80 , C07B61/00 , C07D207/267 , C07D307/08
Abstract: A process for coproducing alkyl-substituted or unsubstituted THF and pyrrolidones by catalytically hydrogenating C 4 -dicarboxylic acids and/or derivatives thereof in the gas phase in the presence of copper catalysts and reacting GBL with ammonia or primary amines to give pyrrolidones comprises a) hydrogenating C 4 -dicarboxylic acids and/or derivatives thereof in the gas phase at from 200 to 300° C., from 0.1 to 100 bar, catalyst hourly space velocities of from 0.01 to 1 kg of reactant/l of catalyst*hour and reactant/hydrogen molar ratios of from 20 to 800 in the presence of catalysts comprising copper, aluminum and/or zinc to give mixtures of THF and GBL, b) separating the hydrogenation effluent obtained by distillation into a THF/water mixture as the top product and a GBL-containing bottom product, c) separating the THF/water mixture from step b) in a distillation facility consisting of three columns by withdrawing water from the bottom of the first column, recycling water-containing THF from the second into the first column, passing a side stream of the first into the second column, recycling the bottom product of the third column into the first column and withdrawing a distillate at the top of the first column, wherein a side stream of the second column is passed into the third column and the pure THF is obtained as the top product of the third column, d) recovering GBL from the GBL-containing bottom product from step b) by distillation and e) reacting the GBL obtained with ammonia or amines to give corresponding pyrrolidones.
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公开(公告)号:ES2236559T3
公开(公告)日:2005-07-16
申请号:ES02758298
申请日:2002-07-03
Applicant: BASF AG
Inventor: SCHLITTER STEPHAN , BORCHERT HOLGER , HESSE MICHAEL , SCHUBERT MARKUS , BOTTKE NILS , FISCHER ROLF-HARTMUTH
IPC: B01J23/89 , B01J37/02 , B01J37/03 , C07D307/08 , C07D307/33 , C07D315/00
Abstract: Catalizador para la hidrogenación de ácidos dicarboxílicos C4 y/o sus derivados, preferentemente, anhídrido maleico, en fase gaseosa, caracterizado porque este catalizador presenta de 40 a 92% en peso de óxido de cobre, de 0, 005 a 5% en peso de paladio y/o un compuesto de paladio, y de 2 a 59, 99% en peso de un material portador oxídico que presenta centros ácidos, seleccionado entre el grupo de los óxidos de Al, Si, Zn, La, Ce, de los elementos de los grupos IIIA a VIIIA, así como de los grupos IA y IIA.
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公开(公告)号:ES2231718T3
公开(公告)日:2005-05-16
申请号:ES02748813
申请日:2002-06-24
Applicant: BASF AG
Inventor: SCHLITTER STEPHAN , SIGWART CHRISTOPH , DORFLINGER WALTER , HESSE MICHAEL , FISCHER ROLF-HARTMUTH
Abstract: Catalizador para la obtención de politetrahidrofurano, copolímeros de politetrahidrofurano, diésteres o monoésteres de estos polímeros mediante polimerización de tetrahidrofurano en presencia de al menos un telógeno y/o comonómero estando presente el mismo en forma de cuerpos moldeados de catalizador o partículas de catalizador con un volumen del cuerpo moldeado o partícula individual de al menos 0, 05 mm3, preferentemente de al menos 0, 2 mm3 y particularmente de 0, 1 mm3 y mostrando este catalizador ambas características a) y b): a)Distribución de radios de poros con al menos un máximo de la distribución de poros en el intervalo de 100 hasta 5000 A de radios de poros, y b)Volumen de poros de poros de catalizador con radios de 2oo a 3000 A mayor que 0, 05 cm3/g y/o radios de 200 a 5000 A mayor que 0, 075 cm3/g y/o un radio de > 200 A mayor que 0, 1 cm3/g.
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公开(公告)号:DE50202060D1
公开(公告)日:2005-02-24
申请号:DE50202060
申请日:2002-07-03
Applicant: BASF AG
Inventor: SCHLITTER STEPHAN , BORCHERT HOLGER , HESSE MICHAEL , SCHUBERT MARKUS , BOTTKE NILS , FISCHER ROLF-HARTMUTH , ROESCH MARKUS , HEYDRICH GUNNAR , WECK ALEXANDER
IPC: B01J23/89 , B01J37/02 , B01J37/03 , C07D307/08 , C07D307/33 , C07D315/00
Abstract: A catalyst (I) for the gas phase hydrogenation of 4C-dicarboxylic acids and/or derivatives, preferably maleic acid anhydride, comprises copper oxide (20-94 wt.%), palladium and/or a palladium compound (0.005-5 wt.%) and an oxide support (2-79.995 wt.%) comprising oxides of Al, Si, Zn, La, Ce, Group IIIa-VIIIa elements and/or Group IA and II elements. Independent claims are also included for: (i) a process for the production of the catalyst (I) by impregnation of an oxide supported copper oxide catalyst with a solution of a soluble palladium compound, drying and optionally calcining; and (ii) a process for the gas phase hydrogenation of 4C-dicarboxylic acids and/or derivatives, preferably maleic acid anhydride in the presence of the catalyst (I).
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公开(公告)号:AT273292T
公开(公告)日:2004-08-15
申请号:AT01984809
申请日:2001-12-07
Applicant: BASF AG
Inventor: BORCHERT HOLGER , SCHLITTER STEPHAN , FISCHER ROLF-HARTMUTH , ROESCH MARKUS , STEIN FRANK , RAHN RALF-THOMAS , WECK ALEXANDER , KAIBEL GERD
IPC: C07B61/00 , C07D307/08 , C07D307/33
Abstract: The present invention relates to a process for the gas-phase hydrogenation of C4-dicarboxylic acids and/or their derivatives over a catalyst based on copper oxide to give substituted or unsubstituted gamma-butyrolactone and/or tetrahydrofuran, which comprises, which a first reaction zone in which the C4-dicarboxylic acid and/or its derivatives is/are reacted to give a mixture comprising a substituted or unsubstituted gamma-butyrolactone as main product and a subsequent second reaction zone in which the substituted or unsubstituted gamma-butyrolactone present in the mixture from the first hydrogenation step is reacted at a temperature lower than the temperature in the first hydrogenation step to give substituted or unsubstituted tetrahydrofuran.
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公开(公告)号:AU2003296717A8
公开(公告)日:2004-07-22
申请号:AU2003296717
申请日:2003-12-21
Applicant: BASF AG
Inventor: HESSE MICHAEL , GRASSLER THOMAS , ZEHNER PETER , SCHLITTER STEPHAN , WECK ALEXANDER , PINKOS ROLF , HAUBNER MARTIN
Abstract: The present invention relates to a process for preparing polytetrahydrofuran, polytetrahydrofuran copolymer, diester or monoester by polymerizing tetrahydrofuran in the presence of at least one telogen and/or comonomer and of an acidic heterogeneous catalyst based on activated sheet silicates or mixed metal oxides in a fluidized bed.
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67.
公开(公告)号:AU2003258701A1
公开(公告)日:2004-04-23
申请号:AU2003258701
申请日:2003-09-04
Applicant: BASF AG
Inventor: KASHAMMER STEFAN , PFAFF KLAUS-PETER , PINKOS ROLF , GERSTLAUER ACHIM , HAUBNER MARTIN , SCHLITTER STEPHAN
IPC: C08G65/20
Abstract: Process for preparation of mono- or diesters of tetrahydrofuran homo- or copolymer by polymerisation of tetrahydrofuran in the presence of at least one telogen and/or comonomers using an acid catalyst where the polymerisation reactor is started with a mixture of polytetrahydrofuran, its mono- or diester and /or tetrahydrofuran copolymer, tetrahydrofuran, optionally a copolymer and at least one carboxylic acid and/or a carboxylic acid anhydride is new.
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公开(公告)号:AU2003251666A1
公开(公告)日:2004-04-08
申请号:AU2003251666
申请日:2003-07-30
Applicant: BASF AG
Inventor: GROLL PETER , SCHLITTER STEPHAN , PFAFF KLAUS-PETER , PINKOS ROLF , KASHAMMER STEFAN , MENGER VOLKMAR , HAUBNER MARTIN
IPC: C07D307/08 , C08G65/20 , C08G65/26
Abstract: A process for the continuous production of tetrahydrofuran (THF) by reaction of a 1,4-butanediol reaction mixture at a heteropolyacid catalyst that has not been pre-dried is characterized in that the reaction mixture contains 2-(4-hydroxybutoxy)tetrahydrofuran.
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公开(公告)号:AU2003258545A1
公开(公告)日:2004-03-19
申请号:AU2003258545
申请日:2003-07-30
Applicant: BASF AG
Inventor: PINKOS ROLF , HESSE MICHAEL , HAUBNER MARTIN , SCHLITTER STEPHAN
IPC: B01J23/80 , B01J37/18 , C08G65/322 , C08G65/331 , C08G65/20 , B01J23/00 , C08G65/10 , C08G65/26
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公开(公告)号:DE10237954A1
公开(公告)日:2004-03-04
申请号:DE10237954
申请日:2002-08-20
Applicant: BASF AG
Inventor: PINKOS ROLF , KAESHAMMER STEFAN , MENGER VOLKMAR , HAUBNER MARTIN , GROLL PETER , SCHLITTER STEPHAN , PFAFF KLAUS-PETER
IPC: C07D307/08 , C08G65/20 , C08G65/26 , C07D307/04
Abstract: A process for the continuous production of tetrahydrofuran (THF) by reaction of a 1,4-butanediol reaction mixture at a heteropolyacid catalyst that has not been pre-dried is characterized in that the reaction mixture contains 2-(4-hydroxybutoxy)tetrahydrofuran.
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