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公开(公告)号:DE50011317D1
公开(公告)日:2005-11-17
申请号:DE50011317
申请日:2000-08-02
Applicant: BASF AG
Inventor: KAIBEL DR , STROEZEL MANFRED , STAMMER DR
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公开(公告)号:DE50102763D1
公开(公告)日:2004-08-05
申请号:DE50102763
申请日:2001-09-19
Applicant: BASF AG
Inventor: KAIBEL GERD , OOST CARSTEN , STROEZEL MANFRED , MEYER GERALD , TRUEBENBACH PETER , SARTOR KARL-HEINZ , HENERS JUERGEN
Abstract: A process is proposed for the separation of C 5+ cuts by distillation into a low-boiler (A), a medium-boiler (B) and a high-boiler fraction (C) in one or more dividing-wall columns (TK), in which a dividing wall (T) is arranged in the longitudinal direction of the column with formation of an upper, common column region ( 1 ), a lower, common column region ( 6 ), a feed part ( 2, 4 ) with rectifying section ( 2 ) and stripping section ( 4 ), and a withdrawal part ( 3, 5 ) with rectifying section ( 5 ) and stripping section ( 3 ), with feed of the C 5+ cut (A, B, C) into the central region of the feed part ( 2, 4 ), discharge of the high-boiler fraction (C) from the bottom of the column, discharge of the low-boiler fraction (A) via the top of the column, and discharge of the medium-boiler fraction (B) from the central region of the withdrawal part ( 3, 5 ), wherein the dividing ratio of the liquid reflux at the upper end of the dividing wall (T) is set in such a way that the proportion of high-boiling key components in the liquid reflux over the stripping section ( 3 ) of the withdrawal part at the upper end of the dividing wall (T) is from 10 to 80%, preferably from 30 to 50%, of the limit value allowed in the medium-boiler fraction (B), and wherein the heating power in the evaporator at the bottom of the dividing-wall column (TK) is set in such a way that the concentration of the low-boiling key components in the liquid at the lower end of the dividing wall (T) is from 10 to 80%, preferably from 30 to 50%, of the limit value allowed in the medium-boiler fraction (B).
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公开(公告)号:AT243072T
公开(公告)日:2003-07-15
申请号:AT97104966
申请日:1997-03-24
Applicant: BASF AG
Inventor: KAIBEL GERD DR , BROECKER FRANZ-JOSEF DR , STROEZEL MANFRED
IPC: B01F5/06 , B01J8/00 , B01J8/06 , B01J8/18 , B01J8/20 , B01J8/22 , B01J8/34 , B01J19/24 , C07C45/62
Abstract: In carrying out reactions in a reactor containing a liquid phase in which a catalyst is suspended, and where a gaseous phase may be present, the liquid and gas phases pass, at least partly, through a device having openings or passages whose hydraulic diameter is 0.5-20 (1-3) mm. Also claimed is the reactor including a device having openings or passages in it built so that liquid or gas flow through it during the reaction.
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公开(公告)号:ES2183038T3
公开(公告)日:2003-03-16
申请号:ES97106627
申请日:1997-04-22
Applicant: BASF AG
Inventor: KAIBEL GERD DR , STROEZEL MANFRED , RHEUDE UDO DR
Abstract: A partitioned column for separating a multi-component mixture into three or more fractions comprises at least one removable partition wall. Also claimed is a process for separating a multi-component mixture into three or more fractions using the above column.
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公开(公告)号:AT224349T
公开(公告)日:2002-10-15
申请号:AT99122636
申请日:1999-11-13
Applicant: BASF AG
Inventor: OOST CARSTEN , STROEZEL MANFRED , ETZRODT HEINZ , WELLER DIETMAR , RHEUDE UDO , KAIBEL GERD , KRUG THOMAS , SPISKE LUISE , JAEDICKE HAGEN
IPC: B01J31/14 , C07B61/00 , C07C45/67 , C07C45/74 , C07C49/203
Abstract: Preparation of unsaturated ketones by reaction of the corresponding alpha , beta -unsaturated alcohol with an alkyl acetoacetate compound in the presence an organo-aluminum catalyst at constant temperature, with separation and continuous removal of CO2 and alcohol formed. Preparation of unsaturated ketones of formula (I) by reaction of the corresponding alpha , beta -unsaturated alcohol of formula (II) with an alkyl acetoacetate compound of formula (III) in the presence of 0.1-5 mole% (based on (III)) of an organo-aluminum catalyst with separation and continuous distillative removal of CO2 and alcohol of formula R3OH formed during reaction, in a reactor containing a fractionation column, where: (A) (II) is added to the reaction mixture together with the organic catalyst without additional solvent and (III) is then added to this mixture; (B) the reaction temperature is kept constant between 175-220 degrees C; (C) the content of (III) is kept at a constant level between 0.1-10 wt.% during the reaction. R1, R3 = 1-4C alkyl; R2 = 4-30C aliphatic, cycloaliphatic or cycloaliphatic-aliphatic; a, b = optional additional bonds.
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66.
公开(公告)号:CA2435918A1
公开(公告)日:2002-08-08
申请号:CA2435918
申请日:2002-01-29
Applicant: BASF AG
Inventor: STROEZEL MANFRED , PETERSEN HERMANN , MUELLER HANS-JOACHIM , KOCH MICHAEL , SCHREYER PETER , SCHWAB EKKEHARD , HAAKE MATHIAS
IPC: B01J21/18 , B01J23/44 , B01J32/00 , B01J35/02 , B01J35/06 , B01J35/10 , C07B35/02 , C07C29/17 , C07C51/487 , C07C63/26
Abstract: The invention relates to a method for cleaning crude terephthalic acid by means of catalytic, hydrogenating aftertreatment using a catalyst material containing at least one hydrogenation metal applied to a carbon carrier consisting of carbon fibres. The invention also relates to a catalyst consisting of the at least one catalyst material containing the at least one hydrogenation metal applied to the carbon fibres, the BET surface of the carbon carrier being
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公开(公告)号:DE10046609A1
公开(公告)日:2002-04-04
申请号:DE10046609
申请日:2000-09-20
Applicant: BASF AG
Inventor: KAIBEL GERD , OOST CARSTEN , STROEZEL MANFRED , MEYER GERALD , TRUEBENBACH PETER , SARTOR KARL-HEINZ , HENERS JUERGEN
IPC: B01D3/14 , B01D3/32 , B01D3/42 , C07B63/00 , C10G7/00 , C10G7/02 , C10G7/12 , C07C7/04 , B01D3/00
Abstract: The invention relates to a method for carrying out the distillative separation of C5+ cuts into a low boiler fraction (A), a medium boiler fraction (B) and into a high boiler fraction (C) inside one or more partition columns (TK). A partition (T) is arranged inside said partition column(s) in a longitudinal direction of the column(s) while forming an upper common column area (1), a lower common column area (6), a feed part (2, 4) having a reinforcing part (2) and stripping part (4), as well as while forming a withdrawal part (3, 5) also having a reinforcing part (5) and stripping part (3). The inventive method involves the following steps: supplying the C5+ cuts (A, B, C) in the middle area of the feed part (2, 4); discharging the high boiler fraction (C) out of the bottom of the column; discharging the low boiler fraction (A) via the top of the column, and; discharging the middle boiler fraction (B) out of the middle area of the withdrawal part (3, 5). The dividing up ratio of the liquid reflux at the upper end of the partition (T) is set such that the proportion of high-boiling key constituents in the liquid reflux above the stripping part (3) of the withdrawal part at the upper end of the partition (T) ranges from 10 to 80 %, preferably, from 30 to 50 % of the limiting value permitted in the middle boiler fraction (B). In addition, the heating capacity in the bottom evaporator of the partition column (TK) is set such that the concentration of the light-boiling key constituents in the liquid at the lower end of the partition (T) ranges from 10 to 80 %, preferably, from 30 to 50 % of the limiting value permitted in the middle boiler fraction (B).
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公开(公告)号:DE59900760D1
公开(公告)日:2002-03-14
申请号:DE59900760
申请日:1999-08-31
Applicant: BASF AG
Inventor: OOST DR , STROEZEL MANFRED , ETZRODT DR , WELLER DR , BOCKSTIEGEL DR , REIMER KLAUS , KAIBEL DR , JAEDICKE DR
IPC: B01J31/14 , B01D3/00 , B01D3/14 , 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:DE10025382A1
公开(公告)日:2001-12-06
申请号:DE10025382
申请日:2000-05-24
Applicant: BASF AG
Inventor: BROECKER FRANZ JOSEF , HAAKE MATHIAS , STROEZEL MANFRED , WOERZ OTTO , SCHWAB EKKEHARD
IPC: B01J12/00 , B01J19/00 , B01J19/24 , C07B61/00 , C07C45/38 , C07C47/21 , F28D9/04 , B01J8/00 , C07B41/06 , C07C45/29 , C07C49/203
Abstract: The invention relates to a device for carrying out, in a substantially isothermal manner, a heterogeneously catalysed reaction in a gas phase with high heat tonality. The inventive device comprises at least one reactor chamber (101) with an inlet (131, 141) and an outlet (143). The reactor chamber is defined by heat dissipating walls, lying at a substantially constant distance of /m and good thermal conductibility; the reaction gas in the reactor chamber flows at a rate of >/= 200 m per m surface area per hour; and a heat exchange medium flows on the side of the reactor wall opposite the reactor chamber.
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公开(公告)号:ES2139993T3
公开(公告)日:2000-02-16
申请号:ES96111235
申请日:1996-07-12
Applicant: BASF AG
Inventor: BROCKER 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
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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