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:
Jan. 22, 2019

Filed:

Feb. 26, 2016
Applicant:

Kuraray Co., Ltd., Kurashiki-shi, JP;

Inventors:

Hiroshi Ozawa, Tainai, JP;

Yasuhito Kitade, Tainai, JP;

Shouji Tanaka, Tainai, JP;

Assignee:

KURARAY Co., Ltd., Kurashiki-shi, JP;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C08F 6/28 (2006.01); C08F 20/14 (2006.01); C08F 2/02 (2006.01); C08F 6/10 (2006.01); C08F 220/14 (2006.01);
U.S. Cl.
CPC ...
C08F 6/28 (2013.01); C08F 2/02 (2013.01); C08F 6/10 (2013.01); C08F 20/14 (2013.01); C08F 220/14 (2013.01); C08F 2400/00 (2013.01);
Abstract

A method for producing a (meth)acrylic resin composition, comprising: continuously feeding reaction starting materials to a tank reactor, the reaction starting materials comprising a polymerizable monomer component, a chain transfer agent and a radical polymerization initiator, the polymerizable monomer component comprising 50 to 100% by mass of methyl methacrylate, 0 to 20% by mass of an acrylic acid alkyl ester and 0 to 30% by mass of an additional monomer; conducting bulk polymerization of the polymerizable monomer component at a polymerization conversion ratio of 40 to 70% by mass to obtain a liquid containing a (meth)acrylic resin; continuously feeding the resulting liquid to a vented extruder to separate volatile component from the (meth)acrylic resin; conducting distillation using an atmospheric distillation column to separate the volatile component into a high boiling fraction (C) and a low boiling fraction (A); and conducting distillation using a vacuum distillation column having a pressure of −50 kPaG to −101 kPaG at the top of the vacuum distillation column to separate the high boiling fraction (C) into a high boiling fraction (C) and a low boiling fraction (A); reusing the low boiling fraction (A) and the low boiling fraction (A) as part of the reaction starting materials.


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