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公开(公告)号:CZ273596A3
公开(公告)日:1998-05-13
申请号:CZ273596
申请日:1996-09-18
Applicant: BASF AG
Inventor: HAMMON ULRICH DR , SCHLIEPHAKE VOLKER DR , PIES WOLFGANG DR , RAUH ULRICH
Abstract: A process for the rectification and sepn. of unsatd. carboxylic acids (I) from the solvents in which (I) are absorbed after the synthesis reaction. The process involves interrupting the rectification and flushing out the rectification column with basic soln.
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公开(公告)号:CZ273496A3
公开(公告)日:1998-05-13
申请号:CZ273496
申请日:1996-09-18
Applicant: BASF AG
Inventor: BAUR KARL GERHARD DR , ANNEN ULRICH DR , EXNER HERBERT DR , FRIED MICHAEL DR , RAUH ULRICH
IPC: C07C67/08 , C07C67/327 , C07C69/54
Abstract: A process for the prodn. of (1-4C alkyl) (meth)acrylate esters (AM/AE) from esters of formula (I) and opt. esters of formula (II), in which R = H or Me; R , R = 1-4C alkyl; n = 0 or more. The process comprises reaction in the liq. phase under reduced pressure in presence of acid, with continuous removal of cleavage prods. Also claimed is a process for the prodn. of (AM/AE) by the acid-catalysed esterification of 1-4C alkanols with (meth)acrylic acid, in which by-prods. (I) and (II) are sepd. from the prod. mixt. and subjected to the above cleavage process, and the cleavage prods. are continuously removed and returned to the esterification process.
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23.
公开(公告)号:CA2259162A1
公开(公告)日:1997-12-24
申请号:CA2259162
申请日:1997-06-19
Applicant: BASF AG
Inventor: RAUH ULRICH , PIES WOLFGANG , HAMMON ULRICH , SCHLIEPHAKE VOLKER
Abstract: In a method for removing low, medium and high-boiling by-products obtained when producing acrylic acids or methacrylic acids, the gaseous low-boiling byproducts are burned, whereby low and medium-boiling by-products hat have been dissolved in water, if desired together with high-boiling by-products that have been treated with the dissolvent, are taken to the burning stage.
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公开(公告)号:MX9604078A
公开(公告)日:1997-03-29
申请号:MX9604078
申请日:1996-09-13
Applicant: BASF AG
Inventor: BAUR KARL GERHARD , ANNEN ULRICH , EXNER HERBERT , FRIED MICHAEL , RAUH ULRICH
IPC: C07C67/327 , C07C67/08 , C07C69/54
Abstract: Un proceso para la preparacion de ésteres de alquilo C1-C4 de ácido (met)acrílico a partir de ésteres de la formula I (Ver Formula); y eventualmente a partir de ésteres de la formula (II) (Ver Formulano alquilo C1-C4, y n es un numero entero > o igual que 0, en la fase líquida y en presencia de un ácido bajo presion reducida y con remocion continua de los productos de disociacion.
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公开(公告)号:DE102005010587A1
公开(公告)日:2006-06-08
申请号:DE102005010587
申请日:2005-03-08
Applicant: BASF AG
Inventor: HABECK THORSTEN , RAUH ULRICH , FRIESE THORSTEN , MARTAN HANS
Abstract: Continuous preparation of alkyl ester of (meth)acrylic acid (A) comprises supplying (meth)acrylic acid, 1-5C alkanol and acid esterifying catalyst (a) to a reaction zone (5,6); adding the discharged reaction mixture to a rectification unit (I); isolating the alkyl ester of (meth)acrylic acid containing in main stream (23) and a sump stream (22); supplying a partial flow of the sump stream; and isolating the separated sump stream (40). Continuous preparation of alkyl ester of (meth)acrylic acid (A) comprises reacting (meth)acrylic acid and 1-5C alkanol in homogeneous, liquid, solvent-free phase with increased temperature and in presence of a acid esterifying catalyst, where (meth)acrylic acid, alkanol and acid esterified catalyst are supplied to a reaction zone (5,6) (that water formed during a retention time are separated rectificative as a component of a alkanol comprising mixture in one of the reaction zone mounted rectification unit (III), in which obtained distillate is isolated in a alkanol containing organic and a water containing aqueous phase, the organic phase is led back into (III) and the aqueous phase is removed, and a reaction mixture (21) is discharged from the reaction zone); initiating the mixture into a rectification unit (I) and the alkyl ester of (meth)acrylic acid containing in main stream (23) and a sump stream (22) are isolated under addition of water; supplying a partial flow of the sump stream (22) from (I) of a residue column unit (IV) comprising a column boiler (61) and recycling into a main stream (29) in (I) and isolating the separated sump stream (40); where (IV) comprises a rectification column (62) in addition to the column boiler, and the ascending vapors from the column boiler are initiated into the rectification column, and resulting liquid at the lowest stage of the rectifying column is led into the column boiler, where the rectification column is operated in a manner, such that the water content of the resulting liquid at the lowest stage is smaller than 0.1 wt.%.
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公开(公告)号:BR0311497A
公开(公告)日:2005-03-15
申请号:BR0311497
申请日:2003-07-09
Applicant: BASF AG
Inventor: HAMMON ULRICH , MESCHKE JOCHEN , RAUH ULRICH , MUELLER-ENGEL KLAUS JOACHIM , SCHLEMMER PETER , SCHLIEPHAKE VOLKER
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公开(公告)号:DE10232482A1
公开(公告)日:2004-01-29
申请号:DE10232482
申请日:2002-07-17
Applicant: BASF AG
Inventor: HAMMON ULRICH , MESCHKE JOCHEN , RAUH ULRICH , MUELLER-ENGEL KLAUS JOACHIM , SCHLEMMER PETER
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公开(公告)号:ES2179397T3
公开(公告)日:2003-01-16
申请号:ES98107290
申请日:1998-04-22
Applicant: BASF AG
Inventor: SCHLIEPHAKE VOLKER DR , HAMMON ULRICH DR , RAUH ULRICH , SCHRAUT ARMIN DR
Abstract: Reactor arrangement comprises at least two tubular reactors filled with solid particles, at least one reactor containing a temperature measuring device. The novelty is that the tubular reactors are arranged so that the ratio of the composition of the solid particles to the free cross-sectional surfaces of each reactor as well as the pressure loss, measured by passing an inert gas proportionally transversal to the free cross-sectional, are equal over each tubular reactor. Also claimed is a process for treating fluid compositions with the production and consumption of thermal energy using the above reactor arrangement.
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公开(公告)号:DK0765854T3
公开(公告)日:2002-06-17
申请号:DK96115457
申请日:1996-09-26
Applicant: BASF AG
Inventor: HAMMON ULRICH DR , SCHLIEPHAKE VOLKER DR , PIES WOLFGANG DR , RAUH ULRICH
Abstract: A process for the rectification and sepn. of unsatd. carboxylic acids (I) from the solvents in which (I) are absorbed after the synthesis reaction. The process involves interrupting the rectification and flushing out the rectification column with basic soln.
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公开(公告)号:DE59704610D1
公开(公告)日:2001-10-18
申请号:DE59704610
申请日:1997-06-19
Applicant: BASF AG
Inventor: SCHLIEPHAKE VOLKER , HAMMON ULRICH , PIES WOLFGANG , RAUH ULRICH
Abstract: In a process for the disposal of low, mediun, and high-boiling secondary components formed during the preparation of (meth)acrylic acid the gaseous low-boiling secondary components are burned, whilst low-boiling and medium-boiling secondary components that are dissolved in water optionally together with high-boiling secondary components treated with solvent are added.
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