Method for producing thermoplastic resin composition

Patent metadata

Field	Value
Publication number	US-9796847-B2
Application number	US-201514715006-A
Country	US
Kind code	B2
Filing date	May 18, 2015
Priority date	May 20, 2014
Publication date	Oct 24, 2017
Grant date	Oct 24, 2017

Abstract

Provided is a thermoplastic resin composition having high flame resistance, high fluidity during injection molding, and improved impact resistance in a molded article. To provide a method for producing a thermoplastic resin composition, the method including a step (1) of obtaining a polyester resin mixture by melt-kneading a crystalline terephthalate-based polyester resin, and a polyester resin A including at least one kind selected from the group consisting of isophthalic acid, orthophthalic acid, naphthalenedicarboxylic acid, anthracene dicarboxylic acid and pyridine dicarboxylic acid as an aromatic dicarboxylic acid component with an extruder, and a step (2) of mixing the polyester resin mixture, a polycarbonate resin, a flame retardant and a toughening agent.

First claim

What is claimed is:

1. A method for producing a thermoplastic resin composition, the method comprising:
a step (1) of obtaining a polyester resin mixture by melt-kneading, with an extruder 70 to 50 parts by weight of a crystalline terephthalate-based polyester resin, and 30 to 50 parts by weight of a polyester resin A, based on the sum of the terephthalate-based polyester resin and the polyester resin A being 100 parts by weight, the polyester resin A including at least one aromatic dicarboxylic acid component selected from the group consisting of isophthalic acid, orthophthalic acid, naphthalenedicarboxylic acid, anthracene dicarboxylic acid and pyridine dicarboxylic acid; and
a step (2) of mixing the polyester resin mixture, a polycarbonate resin, a flame retardant and a toughening agent to produce the thermoplastic resin composition.

2. The production method according to claim 1 , wherein the polyester resin A is a naphthalate-based polyester resin.

3. The production method according to claim 1 , wherein a cylinder temperature of the extruder is 250 to 280° C.

4. The production method according to claim 1 , wherein the melting calorie (ΔH A ) in the DSC melting curve of the polyester resin mixture is 70% or less with respect to the melting calorie (ΔH B ) in the DSC melting curve of the crystalline terephthalate-based polyester resin (ΔH A /ΔH B ≦0.7).

5. The production method according to claim 1 , wherein the crystalline terephthalate-based polyester resin is at least one of polyethylene terephthalate and polybutylene terephthalate, and the polyester resin A is at least one of polyethylene naphthalate and polybutylene naphthalate.

6. The production method according to claim 1 , wherein in the step (1), a metal-based catalyst is added in an amount of 0.05 weight % or less with respect to a total of 100 weight % of the crystalline terephthalate-based polyester resin and the polyester resin A.

7. The production method according to claim 1 , wherein, in step (2),
10 to 90 parts by weight of the polyester resin mixture, and 10 to 90 parts by weight of the polycarbonate resin are mixed based on the sum of the polyester resin mixture and the polycarbonate resin being 100 parts by weight, and
0.5 to 20 parts by weight of a compatibilizing agent, 1 to 40 parts by weight of the flame retardant, 0.1 to 1 part by weight of a drip inhibitor, and 1 to 20 parts by weight of the toughening agent with respect to a total of 100 parts by weight of polyester resin mixture and polycarbonate resin are mixed in the step (2).

8. The production method according to claim 1 , wherein the molecular weight (Mw) of the polycarbonate resin is 20,000 to 70,000.

9. The production method according to claim 1 , wherein the polyester resin A has crystallinity.

Assignees

• Konica Minolta Inc

Inventors

• Nakajima Yo
• Mamino Masashi
• Yu Yiqiang
• Kitani Ryuji

Classifications

• B29C48/40

  using two or more parallel screws {or at least two parallel non-intermeshing screws}, e.g. twin screw extruders · CPC title

• C08L2205/02

  containing two or more polymers of the same C08L -group · CPC title

• B29C48/92

  Measuring, controlling or regulating · CPC title

• C08J2369/00

  Characterised by the use of polycarbonates; Derivatives of polycarbonates · CPC title

• C08J3/203

  Solid polymers with solid and/or liquid additives · CPC title