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公开(公告)号:DE59900645D1
公开(公告)日:2002-02-21
申请号:DE59900645
申请日:1999-05-21
Applicant: BASF AG
Inventor: BRUNNER MELANIE , RAHN RALF-THOMAS , RHEUDE UDO , HENKELMANN JOCHEM
IPC: C07D307/33 , C07D307/32 , C07D315/00
Abstract: Process for producing butyrolactones of the general formula Iwhere R1 and R2 are each hydrogen, alkyl, hydroxyalkyl, substituted or unsubstituted aryl or substituted or unsubstituted trialkylsilyl, by reacting alkynes of the general formula IIwhere R1 and R2 are each as defined above, with carbon monoxide and water in the presence of a rhodium catalyst under pressures from 20 to 300 bar and hydrogenating the unhydrogenated 2(5H)-furanone intermediates comprisesa) reacting the carbonylation reaction mixture with hydrogen at from 150 to 250° C. and from 100 to 300 bar,b) removing the precipitated catalyst and returning it into the carbonylation reaction, andc) subjecting the catalyst-free reaction mixture to a distillation to recover the butyrolactone.
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公开(公告)号:AU7239101A
公开(公告)日:2001-11-20
申请号:AU7239101
申请日:2001-05-03
Applicant: BASF AG
Inventor: KAIBEL GERD , WECK ALEXANDER , RAHN RALF-THOMAS
IPC: B01D3/14 , B01D3/26 , C07C27/28 , C07C29/80 , C07C31/20 , C07D307/08 , C07D307/33
Abstract: In a process for the continuous fractional distillation of mixtures comprising tetrahydrofuran, gamma-butyrolactone and/or 1,4-butanediol to give at least three fractions, the fractionation is carried out in an assembly of distillation columns comprising at least one dividing wall column or at least one assembly of thermally coupled conventional distillation columns.
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公开(公告)号:DE10021703A1
公开(公告)日:2001-11-08
申请号:DE10021703
申请日:2000-05-04
Applicant: BASF AG
Inventor: KAIBEL GERD , WECK ALEXANDER , RAHN RALF-THOMAS
IPC: B01D3/14 , B01D3/26 , C07C27/28 , C07C29/80 , C07C31/20 , C07D307/08 , C07D307/33
Abstract: Continuous distillative separation into at least 3 fractions of mixtures containing tetrahydrofuran (THF), psi -butyrolactone and/or 1,4-butanediol is effected in an arrangement of distillation columns with at least one partition or in an arrangement of heat-coupled conventional distillation columns.
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公开(公告)号:DE19818248A1
公开(公告)日:1999-10-28
申请号:DE19818248
申请日:1998-04-23
Applicant: BASF AG
Inventor: FISCHER ROLF , KAIBEL GERD , PINKOS ROLF , RAHN RALF-THOMAS
IPC: C07C29/149 , C07C29/17 , C07C31/20 , C07C51/16 , C07C67/03 , C07C67/08 , C07C69/60 , C07D307/08 , C07D307/32 , C07D307/33 , C07D315/00 , C07C29/147 , C07C29/74 , C07B41/00
Abstract: Production of butan-1,4-diol (I) and optionally psi -butyrolactone (GBL) and tetrahydrofuran (THF) involves (i) oxidation of n-butane or benzene to a product stream containing maleic anhydride (II); (ii) absorption of (II) with a high-boiling inert solvent (III); (iii) esterification of the resultant liquid (IV) with a 1-5 carbon (C) alcohol (V) to a stream (VI) containing the corresponding diester and (III); and (iv) hydrogenation of (VI) to give a stream containing (I), optionally GBL and THF and (V), which is separated by distillation into valuable products and (V), (V) being recycled to the esterification zone. The novelty is that, before hydrogenation, (VI) is separated by vacuum distillation into the diester and (III), (III) is recycled to the absorption stage and the diester is hydrogenated in the liquid phase on a stationary bed catalyst. Production of butan-1,4-diol (I) and optionally psi -butyrolactone (GBL) and tetrahydrofuran (THF) involves; (i) oxidation of n-butane or benzene to a product stream containing maleic anhydride (II); (ii) absorption of (II) from the product stream with a high-boiling inert solvent (III) in an absorption stage, giving a liquid absorption discharge (IV); (iii) esterification of (IV) with a 1-5 carbon (C) esterification alcohol (V) in an esterification stage to an esterification discharge (VI) containing the corresponding diester and (III); and (iv) hydrogenation of (VI) to give a hydrogenation discharge containing (I), optionally GBL and THF and (V), which is separated by distillation into valuable products and (V), (V) being recycled to the esterification zone. The novelty is that, before hydrogenation, (VI) is separated by vacuum distillation into the diester and (III), (III) is recycled to the absorption stage and the diester is hydrogenated in the liquid phase on a stationary bed catalyst.
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公开(公告)号:CA2647895A1
公开(公告)日:2007-10-18
申请号:CA2647895
申请日:2007-04-03
Applicant: BASF AG
Inventor: HABERLE KARL , DIETSCHE FRANK , RAHN RALF-THOMAS , HARING DIETMAR
Abstract: The invention relates to a bleach system comprising at least one component selected from bleach, bleach activator or bleach catalyst, wherein the bleach system is enveloped with at least one polymer layer and the polymer has urethane and urea groups. The inventive bleach system and detergent formulations comprising this bleach system are suitable for washing or cleaning textiles or dishware.
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26.
公开(公告)号:CA2639995A1
公开(公告)日:2007-08-23
申请号:CA2639995
申请日:2007-02-07
Applicant: BASF AG
Inventor: RAHN RALF-THOMAS , WISSEMEIER ALEXANDER , MAUSS MICHAEL , HUTTENLOCH OLIVER , WEIGELT WOLFGANG , DECK PATRICK , ZERULLA WOLFRAM , PASDA GREGOR
Abstract: Composition comprises at least two different (thio)phosphoric acidtriamide (I). Composition comprises at least two different (thio) phosphoric acidtriamide (I) of formula (R 1R 2N-P(X)(NH 2) 2). Either R 1, R 2H, 1-10C-alkyl-, 3-10C-cycloalkyl-, 6-10C-aryl- or dialkylaminocarbonyl; or N(R 1+R 2) : 5-6 membered optionally saturated heterocycle, optionally containing 1 or 2 heteroatoms that are replaced by N, O or S; and X : O or S. Independent claims are included for: (1) the preparation of the composition comprising mixing at least two (thio)phosphoricacidtriamide together or transferring thiophosphorylchloride with a mixture of at least two different primary- or secondary amine and subsequently with ammonia; and (2) a urea containing fertilizer comprising the composition.
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公开(公告)号:DE10342566A1
公开(公告)日:2005-04-07
申请号:DE10342566
申请日:2003-09-15
Applicant: BASF AG
Inventor: MUELLER-EVERSBUSCH MAYKE , SCHOENFELDER HENDRIK , GEIER REINER , HOELZLE MARKUS , GRASLER THOMAS , KUHRS CHRISTIAN , RAHN RALF-THOMAS
IPC: B01J8/00 , B01J8/18 , C07D251/60
Abstract: Producing melamine by reacting urea at 350-450[deg]C and up to 20 bar in the presence of a catalyst in the form of a fluidized bed comprises using a fluidized bed reactor with a conical base (5). An independent claim is also included for a reactor for carrying out the above process, comprising a product gas outlet (20) in a top section (19) of the reactor and a fluidizing gas inlet (8) located beneath the contents of the reactor, where the reactor is conical.
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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:DE59906265D1
公开(公告)日:2003-08-14
申请号:DE59906265
申请日:1999-04-16
Applicant: BASF AG
Inventor: FISCHER ROLF , KAIBEL GERD , PINKOS ROLF , RAHN RALF-THOMAS
IPC: C07C29/149 , C07C29/17 , C07C31/20 , C07C51/16 , C07C67/03 , C07C67/08 , C07C69/60 , C07D307/08 , C07D307/32 , C07D307/33 , C07D315/00
Abstract: A process for preparing 1,4-butanediol and, if desired, gamma-butyrolactone and THF by oxidizing butane or benzene to form a product stream including maleic anhydride, absorbing maleic anhydride from the product stream with a high-boiling inert solvent in an absorption stage to give a liquid absorption product, esterifying the liquid absorption product with a C1-C5 esterifying alcohol in an esterification stage to form an esterification product comprising the corresponding diester and high-boiling inert solvent, then hydrogenating the esterification product to give a hydrogenation product which comprises the products of value, 1,4-butanediol and, if desired, gamma-butyrolactone and tetrahydrofuran and the esterifying alcohol and which is separated by distillation into the products of value and the esterifying alcohol, and recycling the esterifying alcohol to the esterification zone, which comprises separating the esterification product into the diester and the inert solvent by distillation under reduced pressure prior to the hydrogenation, recycling the inert solvent to the absorption stage, and hydrogenating the diester in the liquid phase over a fixed-bed catalyst.
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公开(公告)号:MXPA02010530A
公开(公告)日:2003-03-10
申请号:MXPA02010530
申请日:2001-05-03
Applicant: BASF AG
Inventor: RAHN RALF-THOMAS
IPC: B01D3/14 , B01D3/26 , C07C27/28 , C07C29/80 , C07C31/20 , C07D307/08 , C07D307/33
Abstract: En un proceso para la destilacion fraccionada continua de mezclas que contienen tetrahidrofurano, y- butirolactona y/o 1,4-butanodiol para obtener cuando menos tres fracciones, la fraccionacion se realiza en un montaje de columnas de destilacion que consiste en cuando menos una columna con pared divisora o cuando menos un montaje de columnas de destilacion convencionales, acopladas termicamente.
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