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公开(公告)号:DE10104224A1
公开(公告)日:2002-08-01
申请号:DE10104224
申请日:2001-01-31
Applicant: BASF AG
Inventor: HAAKE MATHIAS , SCHWAB EKKEHARD , KOCH MICHAEL , MUELLER HANS-JOACHIM , STROEZEL MANFRED
IPC: B01J21/18 , B01J23/44 , B01J32/00 , B01J35/02 , B01J35/06 , B01J35/10 , C07B35/02 , C07C29/17 , C07C51/487 , C07C63/26 , B01J37/00 , C07C31/125
Abstract: A process for the purification of crude terephthalic acid comprises catalytic hydrogenation using a catalyst material (I) comprising a ca bon supported hydrogenation metal whereby the carbon support comprises carbon fibers. Independent claims are included for: (1) the catalyst material (I) whereby the carbon support has a BET surface area of less than 500 Micro 2>/g; (2) a reactor (II) containing a flat catalyst material in the form of cloth, textile and/or felt comprising a hydrogenation metal applied to carbon fibers and having at least two edges opposite to each other to which the catalyst material is stably affixed or containing the catalyst material in the form of parallel fibers or bands; and (3) a process for the selective hydrogenation of carbon-carbon double or triple bonds and/or hydrogenatable functional groups using the catalyst material (I) or reactor (II).
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公开(公告)号:PT983988E
公开(公告)日:2002-06-28
申请号:PT99117101
申请日:1999-08-31
Applicant: BASF AG
Inventor: STROEZEL MANFRED , HEINZ ETZRODT DR , CARSTEN OOST DR , DIETMAR WELLER DR , BERNHARD BOCKSTIEGEL DR , REIMER KLAUS , GERD KAIBEL DR , HAGEN JAEDICKE DR
IPC: B01D3/00 , B01D3/14 , B01J31/14 , B01D3/32 , B01J10/00 , B01J19/24 , C07B61/00 , C07C45/67 , C07C45/68 , C07C45/82 , C07C49/203 , C07C67/54 , C07C69/72
Abstract: Continuous production of 5-alken-2-one or 3,5-alkadien-2-one derivatives (I) by reacting a 1-alken-3-ol or 1-alkyn-3-ol derivative (II) with an alkyl acetoacetate (III) in a fractionation column to form an acetoacetate and alcohol involves (i) removing the alcohol and (ii) contacting the acetoacetate with catalyst in the lower part or bottom of the column to form (I). Continuous production of unsaturated ketones of formula (I) by reacting an unsaturated alcohol of formula (II) with an alkyl acetoacetate of formula (III) in the presence of an organoaluminum catalyst is carried out by: (a) reacting (II) with (III) on the plates of a fractionation column to form the acetoacetate of (II) and an alcohol of formula R OH; (b) removing the alcohol in the overhead stream from the column; (c) contacting the acetoacetate of (II) with the catalyst in the lower part or bottom of the column to form (I) and CO2; (d) removing the CO2 in the overhead stream from the column; and (e) withdrawing (I) in the bottoms stream from the column. R = 1-4C alkyl; R = 1-37C (un)saturated aliphatic hydrocarbyl (optionally substituted by methoxy groups), 4-12C cycloalkyl or 5-30C cycloalkylalkyl; and R = 1-5C alkyl.
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公开(公告)号:ES2146929T3
公开(公告)日:2000-08-16
申请号:ES97100519
申请日:1997-01-15
Applicant: BASF AG
Inventor: KAIBEL GERD DR , RHEUDE UDO DR , STROEZEL MANFRED , GRAAUW JAN DE PROF DR , OLUJIC ZARKO DR , FREY GUNTHER
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公开(公告)号:DE19853908A1
公开(公告)日:2000-06-08
申请号:DE19853908
申请日:1998-12-07
Applicant: BASF AG
Inventor: OOST CARSTEN , STROEZEL MANFRED , ETZRODT HEINZ , WELLER DIETMAR , KAIBEL GERD , JAEDICKE HAGEN
Abstract: Preparation of unsaturated methyl ketones(I), from an unsaturated alcohol(II) and alkyl acetoacetate(III) in the presence of an organo-aluminum catalyst(IV) comprises: (a) supplying (II) and (IV) to a reactor with a distillation column, (b) making temperature to be 170-250 degrees C under elevated pressure, (c) dosing the mixture with (III) and (d) maintaining a constant (III) content of 0.1-10 wt.% during the reaction. Preparation of unsaturated ketones of formula (I) involves reaction of an unsaturated alcohol of formula (II) with an alkyl acetoacetate of formula (III), in presence of 0.1-5 mol. % (based on (II)) of an organo-aluminum compound catalyst (IV), with elimination and distillative separation of the alcohol R3OH formed in the reaction, in a reactor system provided with a distillation column. Reaction is carried out by: (a) supplying (I (which boils at less than 140 degrees C), without a solvent, and (IV) to the reaction vessel, (b) adjusting the temperature to a value as constant as possible in the range 170-250 degrees C under elevated pressure, (c) dosing the mixture with (III) and (d) maintaining a (III) content as constant as possible in the range 0.1-10 wt. % during the reaction. Dotted line = optional bond; R1 = Me or Et; R2, R3 = 1-4C alkyl.
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公开(公告)号:DE59406396D1
公开(公告)日:1998-08-13
申请号:DE59406396
申请日:1994-08-11
Applicant: BASF AG
Inventor: KAIBEL GERD , STROEZEL MANFRED , PFEFFINGER JOACHIM
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公开(公告)号:DE19526473A1
公开(公告)日:1997-01-23
申请号:DE19526473
申请日:1995-07-20
Applicant: BASF AG
Inventor: BROECKER FRANZ JOSEF DR , STROEZEL MANFRED , RHEUDE UDO DR
IPC: B01J23/44 , B01J35/06 , B01J37/02 , C07B61/00 , C07C5/08 , C07C5/09 , C07C11/02 , C07C29/17 , C07C33/02 , C07C35/02
Abstract: Prepn. of alkenes by partial hydrogenation of alkynes in the liq. phase at 20-250 degrees C and 0.3-200 bar partial hydrogen pressure using a palladium catalyst-comprises:(a) the use of a solid bed carrier-supported catalyst obtd. by tempering the carrier material in air, cooling, coating with metallic palladium under vacuum, shaping and processing into monolithic catalyst element; and (b) the addn. of 10-18 ppm carbon monoxide to the hydrogen.
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公开(公告)号:DE4220239C2
公开(公告)日:1996-03-07
申请号:DE4220239
申请日:1992-06-20
Applicant: BASF AG
Inventor: STROEZEL MANFRED , ARNOLD LOTHAR DR , HOERCHER ULRICH DR , ILLGEN WOLFGANG
Abstract: An assembly to make a liquid made of ingredients including gas which may react with each other. The mixing chamber (1) is formed of a symmetrical outer mantle and two end walls (3, 5). Mixer paddles rotate within the chamber, driven by a motor. The novelty is that the mantle has a separate inlet (8, 9) for each ingredient and an outlet (10) for the mixing product; further that there is a flowpath between the two ends walls (3, 5) formed by a circular passage (17). USE/ADVANTAGE - The unit mixes ingredients including gas which may react together. The mixer is of simple construction and makes a very homogenous and stable produce with steady output.
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公开(公告)号:DE50210233D1
公开(公告)日:2007-07-12
申请号:DE50210233
申请日:2002-01-29
Applicant: BASF AG
Inventor: HAAKE MATHIAS , SCHWAB EKKEHARD , KOCH MICHAEL , MUELLER HANS-JOACHIM , STROEZEL MANFRED , PETERSEN HERMANN , SCHREYER PETER
IPC: C07C51/487 , B01J21/18 , B01J23/44 , B01J32/00 , B01J35/02 , B01J35/06 , B01J35/10 , C07B35/02 , C07C29/17 , C07C63/26
Abstract: A process for the purification of crude terephthalic acid comprises catalytic hydrogenation using a catalyst material (I) comprising a ca bon supported hydrogenation metal whereby the carbon support comprises carbon fibers. Independent claims are included for: (1) the catalyst material (I) whereby the carbon support has a BET surface area of less than 500 Micro 2>/g; (2) a reactor (II) containing a flat catalyst material in the form of cloth, textile and/or felt comprising a hydrogenation metal applied to carbon fibers and having at least two edges opposite to each other to which the catalyst material is stably affixed or containing the catalyst material in the form of parallel fibers or bands; and (3) a process for the selective hydrogenation of carbon-carbon double or triple bonds and/or hydrogenatable functional groups using the catalyst material (I) or reactor (II).
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39.
公开(公告)号:ES2236722T3
公开(公告)日:2005-07-16
申请号:ES96113184
申请日:1996-08-16
Applicant: BASF AG
Inventor: STROEZEL MANFRED , BROCKER FRANZ-JOSEF DR , JANSEN HELMUT , KAIBEL GERD DR
Abstract: LA INVENCION SE REFIERE A MATERIAL DE EMPAQUETADO PARA COLUMNAS DE INTERCAMBIO Y PROCEDIMIENTO PARA SU ELABORACION O MANEJO, DONDE UN MATERIAL DE EMPAQUETADO O UN MATERIAL PARA UTILIZACION COMO MATERIAL DE EMPAQUETADO SE TRATA COMO MATERIAL DE PARTIDA PREVISTO EN UNA COLUMNA DE INTERCAMBIO DE SUSTANCIAS DE FORMA FISICA O QUIMICA DE TAL MODO, QUE LA SUPERFICIE DEL MATERIAL DE EMPAQUETADO SE AGRANDA A TRAVES DE LA GENERACION DE UNA RUGOSIDAD MICROSCOPICA CON UN VALOR DE RUGOSIDAD MEDIO R{SUB,A} SEGUN DIN 4768/1 DESDE 0,01 HASTA 10 MICRAS, CON PREFERENCIA DESDE 0,05 HASTA 1 MICRA.
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公开(公告)号:DE59611188D1
公开(公告)日:2005-03-10
申请号:DE59611188
申请日:1996-08-16
Applicant: BASF AG
Inventor: STROEZEL MANFRED , BROECKER DR , JANSEN HELMUT , KAIBEL DR
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