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公开(公告)号:DE10061556A1
公开(公告)日:2002-06-13
申请号:DE10061556
申请日:2000-12-11
Applicant: BASF AG
Inventor: FISCHER ROLF-HARTMUTH , STEIN FRANK , PINKOS ROLF , HESSE MICHAEL , SPRAGUE MICHAEL JOLYON , ROESCH MARKUS , BORCHERT HOLGER , SCHLITTER STEPHAN , RAHN RALF-THOMAS , WECK ALEXANDER
IPC: B01J23/72 , B01J23/80 , C07C27/06 , C07D307/08
Abstract: The invention relates to a method for the production of optionally alkyl-substituted THF. The above is obtained by catalytic hydrogenation of C4-dicarboxylic acids and/or derivatives thereof, in the gas phase, using a catalyst containing 20 wt. %, preferably >30 wt %, in particular 35 to 90 wt. % of an oxidic support with acidic centres, whereby the method is carried out with a hot spot temperature of 240 to 280 DEG C and a catalytic loading of 0.01 to 1.0, preferably 0.02 to 1, in particular 0.05 to 0.5 kg reactant/l catalyst.hour.
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公开(公告)号:DE19823835A1
公开(公告)日:1999-12-02
申请号:DE19823835
申请日:1998-05-28
Applicant: BASF AG
Inventor: LIANG SHELUE , FISCHER ROLF HARTMUTH , STEIN FRANK , WULFF-DOERING JOACHIM
IPC: B01J23/10 , C07B61/00 , C07C45/48 , C07C49/297 , C07C45/54 , C07C49/395
Abstract: The invention relates to a method for producing cyclopentanone by reacting adipic esters of formula (I) R1OOC-(CH2)4-COOR2 in which R1 and R2 represent alkyl radicals having 1 to 12 carbon atoms, cycloalkyl radicals having 5 or 6 carbon atoms, alkyl aryl or aryl radicals, and R2 can represent additional hydrogen, in the presence of oxidic catalysts. According to the inventive method, adipic esters of formula (I) are reacted with less than 5 wt.% of secondary products, said products not being adipic esters in the gas phase when in the presence of water, with a carrier gas, and a) 0.01 to 10 wt.% of at least one metal oxide, selected from the first or second main group of the periodic table or from the group of rare-earth metals, is reacted on titanium oxide or zirconium dioxide acting as a catalyst support, or b) 0.01 to 50 wt.% of at least one metal oxide, selected from the second main group of the periodic table, is reacted on zinc oxide acting as a catalyst support.
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公开(公告)号:CA2297724A1
公开(公告)日:1999-05-27
申请号:CA2297724
申请日:1998-10-16
Applicant: BASF AG
Inventor: PINKOS ROLF , FISCHER ROLF HARTMUTH , STEIN FRANK
IPC: C07B61/00 , C07C29/149 , C07C29/80 , C07C31/20 , C07C51/367 , C07C62/02 , C07C67/31 , C07C69/675
Abstract: The invention relates to a method for producing 1,6-hexanediol and 6hydroxycaproic acid or their esters by the catalytic hydrogenation of adipic acid, adipic acid monoesters or adipic acid diesters or educt flows containing adipic acid or its esters as essential constituents. The bottom product obtained when the hydrogenation discharge is distilled after the hexanediol and the hydroxycaproic acid or its esters have been separated off is reintroduced into the hydrogenation process, said bottom product essentially containing oligomeric esters of the 6-hydroxycaproic acid. The resulting mixture of the educt and the return flow is reacted at temperatures of 100 to 300 ~C and at pressures of 10 to 300 bar in the liquid phase and with a molar ratio of carboxyl groups to be hydrogenated to hydrogen in the reactor of 1:5 to 1:100, on hydrogenating catalysts.
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公开(公告)号:AU5483498A
公开(公告)日:1998-06-29
申请号:AU5483498
申请日:1997-11-18
Applicant: BASF AG
Inventor: ELLER KARSTEN , SIGWART CHRISTOPH , BECKER RAINER , PLITZKO KLAUS-DIETER , FISCHER ROLF , STEIN FRANK , MULLER ULRICH , HESSE MICHAEL
Abstract: Polytetrahydrofuran, tetrahydrofuran copolymers, diesters or monoesters of these polymers are prepared by polymerizing tetrahydrofuran in the presence of at least one telogen and/or comonomer on a heterogeneous carrier catalyst which contains on an oxidic carrier material as active mass a catalytically active amount of at least one oxygenous molybdenum and/or tungsten compound and, when the precursor compounds of the active mass have been applied to the carrier material precursor, has been calcined at temperatures of between 500° C. and 1000° C. The catalyst used contains a promotor which comprises at least one element or a compound of an element of the 2nd, 3rd including the lanthanides, 5th, 6th, 7th, 8th or 14th group of the periodic system of elements.
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公开(公告)号:ES2227309T3
公开(公告)日:2005-04-01
申请号:ES01985854
申请日:2001-12-07
Applicant: BASF AG
Inventor: FISCHER ROLF-HARTMUTH , STEIN FRANK , PINKOS ROLF , HESSE MICHAEL , SPRAGUE MICHAEL JOLYON , RISCH MARKUS
IPC: B01J23/72 , B01J23/80 , C07C27/06 , C07D307/08
Abstract: Procedimiento para la obtención de THF, en caso dado alquilsubstituido, mediante hidrogenado catalítico en la fase gaseosa de ácidos dicarboxílicos con 4 átomos de carbono y/o sus derivados, con un catalizador que contiene 20 % en peso, preferentemente > 30 % en peso, en especial un 35 a un 90 % en peso de un soporte oxídico con centros ácidos, llevándose a cabo el procedimiento a una temperatura Hot- Spot de 240 a 310ºC, preferentemente 240 a 280ºC, y cargas de catalizador de 0, 01 a 1, 0, preferentemente 0, 02 a 1, en especial 0, 05 a 0, 5 kg de educto / l de catalizador * hora.
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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:MY117553A
公开(公告)日:2004-07-31
申请号:MYPI9700831
申请日:1997-03-01
Applicant: BASF AG
Inventor: BREITSCHEIDEL BORIS , STEIN FRANK , RUST HARALD , BAUR KARL GERHARD , FISCHER ROLF , PINKOS ROLF DR
IPC: B01J23/80 , C07C29/149 , B01J23/889 , C07B61/00 , C07C31/20
Abstract: 1,6-HEXANEDIOL IS PREPARED FROM A CARBOXYLIC ACID MIXTURE COMPRISING ADIPIC ACID, 6-HYDROXYCAPROIC ACID AND SMALL AMOUNTS OF 1,4- CYCLOHEXANEDIOLS WHICH IS OBTAINED AS A BY-PRODUCT IN THE OXIDATION OF CYCLOHEXANE TO CYCLOHEXANONE/CYCLOHEXANOL BY WATER EXTRACTION OF THE REACTION MIXTURE, BY ESTERIFICATION OF THE ACIDS AND HYDROGENATION WHEREIN A) THE MONOCARBOXYLIC AND DICARBOXYLIC ACIDS PRESENT IN THE AQUEOUS DICARBOXYLIC ACID MIXTURE ARE REACTED WITH A LOW MOLECULAR WEIGHT ALCOHOL TO GIVE THE CORRESPONDING CARBOXYLIC ESTERS, B) THE RESULTING ESTERIFICATION MIXTURE IS FREED OF EXCESS ALCOHOL AND LOW BOILERS IN A FIRST DISTILLATION STAGE, C) THE BOTTOMS ARE FRACTIONATED IN A SECOND DISTILLATION STAGE TO GIVE AN ESTER FRACTION ESSENTIALLY FREE OF 1,4-CYCLOHEXANEDIOSL AND A FRACTION COMPRISING AT LEAST THE MAJOR PART OF THE 1,4-CYCLOHEXANEDIOLS, D) THE ESTER FRACTION ESSENTIALLY FREE OF 1,4-CYCLOHEXANEDIOLS IS CATALYTICALLY HYDROGENATED AND E) IN A PURE DISTILLATION STAGE, 1,6-HEXANEDIOL IS ISOLATED FROM THE HYDROGENATION PRODUCT IN A MANNER KNOWN PER SE. 3
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公开(公告)号:DE59905197D1
公开(公告)日:2003-05-28
申请号:DE59905197
申请日:1999-05-10
Applicant: BASF AG
Inventor: STEIN FRANK , KRUG THOMAS , GALL MARTIN , IFFLAND GABRIELE
IPC: C07C29/149 , C07C31/20 , C07C51/47 , C07C67/03 , C07C67/56 , C07C69/44 , C07C69/675
Abstract: A process for preparing 1,6-hexanediol from a carboxylic acid mixture obtained as by-product in the oxidation of cyclohexane to cyclohexanone/cyclohexanol with oxygen or oxygen-comprising gases and by aqueous extraction of the reaction mixture and comprising adipic acid, 6-hydroxycaproic acid and small amounts of 1,4-cyclohexanediols by esterification of the acids and hydrogenation, bya) reacting the mono- and dicarboxylic acids in the aqueous dicarboxylic acid mixture with a low molecular weight alcohol to form the corresponding carboxylic esters,b) conducting a first distillation to remove excess alcohol and low boilers from the esterification mixture obtained,c) conducting a second distillation to separate the bottom product into an ester fraction which is essentially free from 1,4-cyclohexanediols and a fraction which includes at least the larger proportion of the 1,4-cyclohexanediols,d) subjecting the ester fraction essentially free from 1,4-cyclohexanediols to a catalytic hydrogenation, ande) subjecting the hydrogenation effluent to a distillation to recover 1,6-hexanediol in a conventional manner,comprises using an aqueous dicarboxylic acid mixture comprising more than 20 ppm of cobalt and more than 40 ppm of phosphorus in the form of phosphate and passing this aqueous dicarboxylic acid mixture through a cation exchanger and after the esterification of step (a) through an anion exchanger.
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公开(公告)号:DE59807875D1
公开(公告)日:2003-05-15
申请号:DE59807875
申请日:1998-05-06
Applicant: BASF AG
Inventor: ELLER KARSTEN , STEIN FRANK , SIGWART CHRISTOPH , BECKER RAINER , PLITZKO KLAUS-DIETER , FISCHER ROLF , MUELLER ULRICH
Abstract: A process for polymerizing cyclic ethers over a heterogeneous catalyst comprises using a heterogeneous catalyst comprising one or more pillared interlayered clays (PILCs).
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公开(公告)号:ES2174528T3
公开(公告)日:2002-11-01
申请号:ES98963560
申请日:1998-12-10
Applicant: BASF AG
Inventor: BREITSCHEIDEL BORIS , PINKOS ROLF , STEIN FRANK , LIANG SHELUE , FISCHER ROLF HARTMUTH
IPC: C07B61/00 , C07C29/149 , C07C31/20
Abstract: A process for producing 1,6-hexanediol by hydrogenation of adipic esters and/or 6-hydroxycaproic esters in the gas phase at elevated temperature and elevated pressure in the presence of chromium-free catalysts comprises hydrogenatinga) over a catalyst comprising copper, manganese and aluminum as essential constituents or over Raney copper,b) at a temperature of from 150 to 230° C. and a pressure of from 10 to 70 bar,c) at a molar ratio of hydrogen to ester to be hydrogenated within the range from 150:1 to 300:1, andd) at a catalyst space velocity of from 0.01 to 0.3 kg of C6 ester per liter of catalyst per hour.
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