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:
Apr. 29, 2014

Filed:

Apr. 22, 2010
Applicants:

Willibald Dafinger, Röhrnbach, DE;

Peter Holl, Emmerting, DE;

Johann Wagner, Burghausen, DE;

Inventors:

Willibald Dafinger, Röhrnbach, DE;

Peter Holl, Emmerting, DE;

Johann Wagner, Burghausen, DE;

Assignee:

Wacker Chemie AG, Munich, DE;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C07C 67/05 (2006.01);
U.S. Cl.
CPC ...
C07C 67/05 (2013.01);
Abstract

The invention relates to a method for producing vinyl acetate in a heterogeneously catalyzed, continuous gas-phase process by reacting ethylene with acetic acid and oxygen in a reactor, and a) separating the product gas flow essentially containing ethylene, vinyl acetate, acetic acid, water, carbon dioxide, and other inert gases, and b) feeding a circulating gas flow containing ethylene and COback into the reactor, c) the circulating gas flow being compressed in a circulating gas compressor before being fed back into the reactor, and d) a partial flow of the circulating gas is branched off on the suction side or the pressure side of the circulating gas compressor and is fed to a COscrubbing process, and e) is scrubbed in a water scrubber before the COscrubbing process, characterized in that f) after the COscrubbing process, the partial flow, together with ethylene as a propellant, is fed, by means of a jet compressor, to the circulating gas on the pressure side of the circulating gas compressor and downstream of the point where the partial flow is removed for COscrubbing, and/or g) the bottom product from the water scrubber is fed directly to the pre-dehydration column.


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