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:
Jun. 23, 2015

Filed:

May. 31, 2012
Applicants:

Hans-peter Weitzel, Reischach, DE;

Bernhard Eckl, Burghausen, DE;

Dorothee Guenaltay, Emmerting, DE;

Inventors:

Mehmet Guenaltay, Emmering, DE;

Hans-Peter Weitzel, Reischach, DE;

Bernhard Eckl, Burghausen, DE;

Assignee:

Wacker Chemie AG, Munich, DE;

Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
B01D 19/00 (2006.01); C02F 1/20 (2006.01); B01D 3/00 (2006.01); C02F 1/00 (2006.01); C02F 1/04 (2006.01); C08F 6/00 (2006.01); C08J 11/02 (2006.01); C02F 103/38 (2006.01);
U.S. Cl.
CPC ...
C02F 1/20 (2013.01); B01D 3/00 (2013.01); C02F 1/00 (2013.01); C02F 1/04 (2013.01); C02F 2103/38 (2013.01); C08F 6/003 (2013.01); C08F 6/006 (2013.01); C08J 11/02 (2013.01);
Abstract

A method for processing wastewater and exhaust gas condensates from the polymerization of vinyl acetate and ethylene and optionally other comonomers in an aqueous medium by suspension or emulsion polymerization employs relieving pressure after completion of the polymerization of the polymerization batch and discharging the polymer dispersion. During the relieving, the gaseous phase is removed by means of a compressor. Optionally, the gaseous phase occurring during stripping is removed by the compressor and cooled by one or more heat exchangers before entry into the compressor. The liquid phases occurring in the compressor and optionally in the heat exchanger are separated from the gaseous phase and the liquid phases are given to a rectification column, and separated into a vinyl acetate monomer phase and a wastewater phase, and the vinyl acetate monomer phase is resupplied to polymerization.


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