The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.

The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.

Date of Patent:
May. 28, 2019

Filed:

Nov. 28, 2016
Applicant:

Basf SE, Ludwigshafen am Rhein, DE;

Inventors:

Catharina Horstmann, Ludwigshafen am Rhein, DE;

Claus Hechler, Ludwigshafen am Rhein, DE;

Gregor Grackiewicz, Ludwigshafen am Rhein, DE;

Bernd Schall, Ludwigshafen am Rhein, DE;

Assignee:

BASF SE, Ludwigshafen Am Rhein, DE;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01D 3/00 (2006.01); B01D 3/14 (2006.01); B01D 5/00 (2006.01); C07C 67/02 (2006.01); C07C 67/04 (2006.01); C07C 67/54 (2006.01); C07C 67/62 (2006.01); C07C 69/54 (2006.01);
U.S. Cl.
CPC ...
C07C 67/54 (2013.01); B01D 3/009 (2013.01); B01D 3/143 (2013.01); B01D 5/006 (2013.01); C07C 67/02 (2013.01); C07C 67/04 (2013.01); C07C 67/62 (2013.01); C07C 69/54 (2013.01); B01D 3/148 (2013.01); Y02P 20/127 (2015.11);
Abstract

A process for continuously preparing the tert-butyl ester of an ethylenically unsaturated carboxylic acid, by a) reacting an ethylenically unsaturated carboxylic acid with isobutene in the presence of an acidic catalyst to give an esterification mixture; b) removing the acidic catalyst; c) removing low-boiling components; and d) supplying a tert-butyl ester-comprising liquid to a distillation apparatus and subjecting it to purifying distillation in the distillation apparatus, where d1) in the distillation apparatus the tert-butyl ester-comprising liquid is separated into a tert-butyl ester-comprising gaseous top product and a carboxylic acid-comprising liquid bottom product; d2) the tert-butyl ester-comprising gaseous top product is at least partly condensed and the condensate is recycled partly as reflux to the distillation apparatus; d3) the carboxylic acid-comprising liquid bottom product is recycled at least partly to step a); d4) carboxylic acid-comprising liquid bottom product is drawn off and passed to a heater; a superheated, liquid recycle stream is taken from the heater; and the superheated recycle stream is let down into the distillation apparatus; and d5) at least in the top region of the distillation apparatus, the distillation apparatus walls in contact with the vapor, at least in sub-regions, are heated and/or thermally insulated. In the course of the process, the separation of the tert-butyl ester from unreacted carboxylic acid is carried on with a particularly low level of accompanying polymerization both of the tert-butyl ester and of the carboxylic acid.


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