Polyphenylene sulfide resin composition, method of producing same, and molded article

A method of producing the polyphenylene sulfide resin composition which comprises:

• 99.5 to 51 parts by weight of a polyphenylene sulfide resin (A);
• 0.5 to 49 parts by weight of an aromatic vinyl compound block copolymer (B) containing at least one functional group selected from the group consisting of a carboxyl group, an acid anhydride group, a hydroxyl group, an amino group, an epoxy group and an isocyanate group;
• and
• 0.1 to 2.0 parts by weight, with respect to 100 parts by weight of the total amount of said polyphenylene sulfide resin (A) and said aromatic vinyl compound block copolymer (B), of an alkoxy silane compound (C) containing at least one functional group selected from the group consisting of an epoxy group, an amino group and an isocyanate group;
• wherein a phase structure of said polyphenylene sulfide resin composition is a sea-island structure in which said polyphenylene sulfide resin (A) forms a sea phase, and said aromatic vinyl compound block copolymer (B) forms an island phase dispersed in a number average dispersed particle size of 1,000 nm or less,
• the method comprising:
• performing melt-kneading using a twin screw extruder having a ratio L/D of screw length L to screw diameter D of 10 or more, at a melt-kneading energy E (kWh/kg), represented by equation (2), of 0.15 kWh/kg or more and 0.50 kWh/kg or less:
• E={(A/B)×C}/F (2)
• wherein A represents a screw rotation speed (rpm) of said twin screw extruder during the melt-kneading;
• B represents a maximum screw rotation speed (rpm) of said twin screw extruder;
• C represents an output (kW) of a screw drive motor during the melt-kneading;
• and F represents a discharge amount (kg/h) of a molten resin during the melt-kneading,
• wherein said twin screw extruder includes:
• a cylinder;
• a main feed port provided to said cylinder;
• and
• a side feed port provided on a downstream side of said main feed port in an extrusion direction;
• wherein said aromatic vinyl compound block copolymer (B) is fed from said side feed port, and
• 80% to 98% by weight of the total amount of said aromatic vinyl compound block copolymer (B) is fed from said side feed port, and 2 to 20% by weight of said aromatic vinyl compound block copolymer (B) is fed from said main feed port.