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:
Nov. 27, 2018

Filed:

Nov. 16, 2015
Applicant:

Covestro Deutschland Ag, Leverkusen, DE;

Inventors:

Thomas Ernst Müller, Aachen, DE;

Christoph Gürtler, Köln, DE;

Matthias Wohak, Dormagen, DE;

Jörg Hofmann, Krefeld, DE;

Carlson Torren, Newark, DE (US);

Assignee:

Covestro Deutschland AG, Leverkusen, DE;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C08G 64/34 (2006.01); C08G 65/26 (2006.01);
U.S. Cl.
CPC ...
C08G 65/2663 (2013.01); C08G 64/34 (2013.01); C08G 65/2603 (2013.01); C08G 65/2696 (2013.01);
Abstract

The invention relates to a method for producing polyether carbonate polyols, comprising the step of reacting alkylene oxide with carbon dioxide in the presence of an h-functional starter compound and double metal cyanide catalyst. The invention is characterized in that the method comprises the following steps: (α) optionally, pre-treating the double metal cyanide catalyst (DMC catalyst) at a temperature of 50 to 200° C. and/or reduced pressure (absolute) of 10 mbar to 800 mbar; (β) bringing the double metal cyanide catalyst in contact with suspension means, and furthermore, with alkylene oxide in the first reactor thus obtaining a first reaction mixture, and (γ) continuous added dosing of the first reaction mixture, alkaline oxide, and carbon oxide, and optionally, h-functional starter compound in a second reactor, wherein in at least one of the steps (β) or (γ), at least one h-functional starter compound is used, and wherein reaction products formed in step (γ) are continuously removed from the second reactor.


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