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:
Dec. 28, 2010

Filed:

Aug. 13, 2005
Applicants:

Juan Herguijuela, Auggen, DE;

Werner Pietzonka, Therwil, CH;

Angela Wildermann, Bad Säckingen, DE;

Thomas Wolf, Rheinfelden, DE;

Inventors:

Juan Herguijuela, Auggen, DE;

Werner Pietzonka, Therwil, CH;

Angela Wildermann, Bad Säckingen, DE;

Thomas Wolf, Rheinfelden, DE;

Assignee:

DSM IP Assets B.V., Heerlen, NL;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C07D 311/00 (2006.01); B01D 3/14 (2006.01);
U.S. Cl.
CPC ...
Abstract

According to the invention, a process for the rectification of mixtures of high-boiling air- and/or temperature-sensitive substances which require a high separation efficiency is proposed, in particular a process for the working-up of a VE- or VEA-containing product stream. The process is characterized in particular in that, in a first purification stage, low-boiling products and unspecified isomers of the useful product are separated from the product stream virtually without loss of useful product and that, in a second purification stage, the useful product is removed in a stream having a purity of >97% by weight and a further stream having a purity of >92% by weight. A preferred embodiment of the process serves for working up VEA, in which the loss of useful product in the first purification stage is less than 5%, based on that amount of VEA in the feed which is added to the purification stage per unit time. Furthermore, the first purification stage may comprise a rectification column (), from the top (Ia) of which the low-boiling products and the unspecified isomers of VEA are taken off, a stream containing the useful product in purified form being taken off at the side () and/or at the bottom (Ib) of the column ().


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