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. 05, 2024

Filed:

Sep. 17, 2020
Applicant:

Ineos Styrolution Group Gmbh, Frankfurt am Main, DE;

Inventors:

Norbert Niessner, Friedelsheim, DE;

Bianca Wilhelmus, Hanau, DE;

Achim Schmidt-Rodenkirchen, Bayreuth, DE;

Konstantin Mierdel, Bayreuth, DE;

Frank Neuner, Bayreuth, DE;

Assignee:

INEOS STYROLUTION GROUP GMBH, Frankfurt am Main, DE;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C07C 4/22 (2006.01); B01J 8/24 (2006.01); C08J 11/12 (2006.01);
U.S. Cl.
CPC ...
C07C 4/22 (2013.01); B01J 8/24 (2013.01); C08J 11/12 (2013.01); C07C 2601/16 (2017.05); C08J 2325/06 (2013.01); C08J 2423/06 (2013.01); C08J 2423/12 (2013.01); C08J 2455/02 (2013.01); C08J 2467/02 (2013.01);
Abstract

The invention relates to a method for producing styrene monomers by the depolymerisation of polystyrene in the presence of foreign polymers, such as polyolefins. Said method comprises the following steps: a) introducing a polymer composition (A) containing: I) 10 to 99.5% by weight, based on the polymer composition (A), of polystyrene (I); and II) 0.1 to 89.9% by weight of polyolefin (II); and/or III) 0.1 to 4.9% by weight of acrylonitrile-based polymer (III); and/or IV) 0.1 to 4.9% by weight of polyester (IV), into the reaction zone (R) of a pyrolysis reactor (P); b) thermal cracking the polystyrene contained in the polymer composition (A) in the reaction zone (R) of the pyrolysis reactor (P) at a temperature of between 400-1000° C., c) removing the product mixture (G) obtained from the reaction zone (R), d) cooling of the product mixture (G), and e) separating the styrene monomers from the further components.


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