JP2010261018A - Polycarbonate/polyethylene terephthalate composite resin composition, and molded product - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To suppress staying thermal deterioration and to improve molding stability in a polycarbonate resin/polyethylene terephthalate resin composite resin composition. <P>SOLUTION: In the polycarbonate/polyethylene terephthalate composite resin composition, 0.01-0.5 pt.mass of a phosphor-based thermostabilizer and/or 0.01-1 pt.mass of a hindered phenol-based thermostabilizer, 1-10 pts.mass of an elastomer and 1-20 pts.mass of an inorganic filler are formulated to 100 pts.mass of a resin component comprising 95-30 mass% of a polycarbonate resin and 5-70 mass% of a polyethylene terephthalate resin. The polyethylene terephthalate resin is a polyethylene terephthalate resin in which deactivation treatment of a polycondensation catalyst is performed. <P>COPYRIGHT: (C)2011,JPO&INPIT

Description

  The present invention relates to a polycarbonate / polyethylene terephthalate composite resin composition having improved thermal stability and molding stability in a resin composition in which a polyethylene terephthalate resin is combined with a polycarbonate resin for the purpose of imparting chemical resistance. The present invention relates to a molded article formed by molding a polyethylene terephthalate composite resin composition.

  Polycarbonate resins, especially aromatic polycarbonate resins, are excellent in impact resistance, heat distortion resistance, rigidity, dimensional stability, etc., and are therefore used in a wide range of applications such as electrical equipment, communication equipment, precision machinery, and automotive parts. However, the polycarbonate resin has the disadvantage that it is inferior in chemical resistance, and in order to improve the chemical resistance of the polycarbonate resin, various composites with a polyethylene terephthalate resin have been studied (for example, Patent Documents 1 and 2). reference).

  However, when a polyethylene terephthalate resin is compounded with a polycarbonate resin, the chemical resistance is improved, but the resulting resin composition has poor thermal stability and is held at a high temperature in the cylinder during the molding process. And a transesterification reaction with polyethylene terephthalate resin, and generation of decomposition gas due to the reaction causes bubbles and poor appearance of molded products called silver. And, such a decrease in the molecular weight of the polycarbonate resin not only impairs the original impact resistance, heat distortion resistance, etc. of the polycarbonate resin, but also causes a change in viscosity of the polycarbonate resin composition due to retention at a high temperature. Molding stability is impaired, and problems such as short shots and burrs occur in the molded product.

Japanese Patent Laid-Open No. 2007-23118 JP 2009-1620 A

  The present invention solves the above-mentioned conventional problems, and suppresses the residence heat deterioration in the polycarbonate resin / polyethylene terephthalate resin composite resin composition and improves the molding stability and the polycarbonate / polyethylene terephthalate composition. It aims at providing the molded article formed by shape | molding a composite resin composition.

  As a result of intensive studies to solve the above problems, the present inventors have found that the above-mentioned problem of residence heat deterioration in the polycarbonate resin / polyethylene terephthalate resin composite resin composition is used in the production process of polyethylene terephthalate resin and provided as a product. This is due to the polycondensation catalyst contained in the polyethylene terephthalate resin. Therefore, the polyethylene terephthalate resin in which the polycondensation catalyst is deactivated is used as the polyethylene terephthalate resin, and a specific heat stabilizer is blended. As a result, it has been found that deterioration of staying heat can be more reliably suppressed. Furthermore, it has been found that by blending a specific amount of elastomer and an inorganic filler, it is possible to suppress the viscosity change at the time of residence and to improve the molding stability.

  The present invention has been achieved based on such findings, and the gist thereof is as follows.

[1] To 100 parts by mass of a resin component consisting of 95 to 30% by mass of a polycarbonate resin and 5 to 70% by mass of a polyethylene terephthalate resin, 0.01 to 0.5 parts by mass of a phosphorus-based heat stabilizer and / or a hindered phenol type 0.01 to 1 part by mass of a heat stabilizer, 1 to 10 parts by mass of an elastomer and 1 to 20 parts by mass of an inorganic filler were blended, and the polyethylene terephthalate resin was subjected to deactivation treatment of the polycondensation catalyst. A polycarbonate / polyethylene terephthalate composite resin composition, which is a polyethylene terephthalate resin.

[2] In [1], the polyethylene terephthalate resin in which the polycondensation catalyst is deactivated has a terminal carboxyl group concentration of 5 to 40 μeq / g and an intrinsic viscosity [η] of 0.6 to 1.5 dl / g. The ratio of the oxyethylene oxyterephthaloyl unit to all the structural repeating units is 90 equivalent% or more, and the solid phase polymerization rate Ks calculated by the following formula (1) is 0.006 (dl / g · hr) or less. A polycarbonate / polyethylene terephthalate composite resin composition characterized by being.
Solid-phase polymerization rate Ks = ([η] s− [η] m) / T (1)
(Where [η] s is the intrinsic viscosity (dl / g) of the polyethylene terephthalate resin after holding the polyethylene terephthalate resin at 210 ° C. for 3 hours under a nitrogen stream, and [η] m is the polyethylene (The intrinsic viscosity (dl / g) of the polyethylene terephthalate resin after the terephthalate resin is held at 210 ° C. for 2 hours under a nitrogen stream. T is 1 (hour).)

[3] A polycarbonate / polyethylene terephthalate composite resin composition according to [1] or [2], wherein the elastomer is a core / shell type elastomer.

[4] The polycarbonate / polyethylene terephthalate composite resin composition according to [3], wherein a shell portion of the core / shell type elastomer is a polymethyl methacrylate-based polymerized or copolymerized block.

[5] The polycarbonate / polyethylene terephthalate composite resin composition according to any one of [1] to [4], wherein the inorganic filler is a glass fiber.

[6] The polycarbonate / polyethylene terephthalate composite resin composition according to [5], wherein the glass fiber has a glycidyl group on the surface.

[7] As a resin component, it contains 95 to 30% by mass of a polycarbonate resin and 5 to 70% by mass of a polyethylene terephthalate resin, and 1 to 10 parts by mass of an elastomer and 1 to 1 part of an inorganic filler with respect to 100 parts by mass of the resin component. a polycarbonate / polyethylene terephthalate composite resin composition comprising 20 parts by weight, number average molecular weight Mn _x chloroform solubles was held 60 minutes at 280 ° C. is before the 60 minute hold at 280 ° C. chloroform solubles the number average molecular weight Mn of polycarbonate / polyethylene terephthalate composite resin composition which is characterized in that 80% or more _o the.

[8] As a resin component, it contains polycarbonate resin 95 to 30% by mass and polyethylene terephthalate resin 5 to 70% by mass, 1 to 10 parts by mass of elastomer and 1 to 1 part of inorganic filler with respect to 100 parts by mass of the resin component. a polycarbonate / polyethylene terephthalate composite resin composition comprising 20 parts by weight, 280 Charpy impact strength Ip _x after holding for 60 minutes at ° C. is, 280 ° C. at 60 minutes more than 80% of the previous Charpy impact strength Ip _o holding A polycarbonate / polyethylene terephthalate composite resin composition characterized in that:

[9] As a resin component, it contains 95 to 30% by weight of a polycarbonate resin and 5 to 70% by weight of a polyethylene terephthalate resin, and 1 to 10 parts by weight of an elastomer and 1 to 1 part of an inorganic filler with respect to 100 parts by weight of the resin component. A polycarbonate / polyethylene terephthalate composite resin composition containing 20 parts by mass, wherein the resin composition is held at 280 ° C. for 30 minutes and then an injection molded MFR is [R _x ], and the resin composition is injection molded When the MFR of the molded product immediately injection-molded after injection into the machine is [R _o ], the decrease rate of MFR [R _x ] with respect to MFR [R _o ] calculated by the following formula (3) is -20 to 20%. A polycarbonate / polyethylene terephthalate composite resin composition characterized in that:
Reduction rate of MFR [%] = (R _o −R _x ) / R _o × 100 (3)

[10] A polycarbonate / polyethylene terephthalate composite resin molded article obtained by molding the polycarbonate / polyethylene terephthalate composite resin composition according to any one of [1] to [9].

  According to the present invention, a polycarbonate terephthalate resin for imparting chemical resistance to a polycarbonate resin, an elastomer for imparting impact resistance, and an inorganic filler for imparting rigidity and heat resistance are combined. Thus, there is provided a polycarbonate / polyethylene terephthalate composite resin composition that suppresses residence heat deterioration and suppresses a change in viscosity, and has excellent thermal and molding stability and mechanical property balance such as Charpy impact strength and elastic modulus. The

  Such a polycarbonate / polyethylene terephthalate (PC / PET) composite resin composition of the present invention is used for various electrical and electronic equipment parts, OA equipment, machine parts, vehicle parts, building members, various containers, leisure goods and miscellaneous goods, etc. It is useful for applications, and can be expected to be applied especially to vehicle exterior / skin parts and vehicle interior parts.

  Examples of vehicle exterior / skin parts to which the PC / PET composite resin composition of the present invention is applied include outer door handles, bumpers, fenders, door panels, trunk lids, front panels, rear panels, roof panels, bonnets, pillars, side moldings. , Garnish, wheel cap, hood bulge, fuel lid, various spoilers, motorbike cowl, etc.

  In addition, examples of vehicle interior parts include inner door handles, center panels, instrument panels, console boxes, luggage floor boards, display housings for car navigation, etc., and application of the PC / PET composite resin composition of the present invention. The field is not limited to these.

  Hereinafter, embodiments of the present invention will be described in detail. In the present specification, “to” is used to mean that the numerical values described before and after it are included as a lower limit value and an upper limit value.

[Polycarbonate resin]
Examples of the polycarbonate resin used in the PC / PET composite resin composition of the present invention include aromatic polycarbonate resins, aliphatic polycarbonate resins, and aromatic-aliphatic polycarbonate resins, and aromatic polycarbonate resins are preferred.

  The aromatic polycarbonate resin is an optionally branched aromatic polycarbonate polymer obtained by reacting an aromatic hydroxy compound with a phosgene or carbonic acid diester. The method for producing the aromatic polycarbonate resin is not particularly limited, and may be a conventional method such as a phosgene method (interfacial polymerization method) or a melting method (transesterification method). Further, it may be a polycarbonate resin produced by a melting method and produced by adjusting the amount of OH groups of terminal groups.

Typical examples of the aromatic dihydroxy compound that is one of the raw materials of the aromatic polycarbonate resin used in the present invention include, for example, bis (4-hydroxyphenyl) methane and 2,2-bis (4-hydroxyphenyl). Propane, 2,2-bis (4-hydroxy-3-methylphenyl) propane, 2,2-bis (4-hydroxy-3-tert-butylphenyl) propane, 2,2-bis (4-hydroxy-3, 5-dimethylphenyl) propane, 2,2-bis (4-hydroxy-3,5-dibromophenyl) propane, 4,4-bis (4-hydroxyphenyl) heptane, 1,1-bis (4-hydroxyphenyl) Cyclohexane, 4,4′-dihydroxybiphenyl, 3,3 ′, 5,5′-tetramethyl-4,4′-dihydroxybiphenyl, bis (4- Hydroxyphenyl) sulfone, bis (4-hydroxyphenyl) sulfide, bis (4-hydroxyphenyl) ether, bis (4-hydroxyphenyl) ketone and the like.
Furthermore, polyvalent phenols having three or more hydroxy groups in the molecule such as 1,1,1-tris (4-hydroxylphenyl) ethane (THPE), 1,3,5-tris (4-hydroxyphenyl) benzene Etc. can be used together in small amounts as a branching agent.
Among these aromatic dihydroxy compounds, 2,2-bis (4-hydroxyphenyl) propane (hereinafter also referred to as “bisphenol A” and sometimes abbreviated as “BPA”) is preferable. These aromatic dihydroxy compounds can be used alone or in admixture of two or more.

  In order to obtain a branched aromatic polycarbonate resin, phloroglucin, 4,6-dimethyl-2,4,6-tris (4-hydroxyphenyl) heptene-2, 4,6-dimethyl-2,4,6-tris ( 4-hydroxyphenyl) heptane, 2,6-dimethyl-2,4,6-tris (4-hydroxyphenyl) heptene-3, 1,3,5-tris (4-hydroxyphenyl) benzene, 1,1,1 -Polyhydroxy compounds such as tris (4-hydroxyphenyl) ethane, or 3,3-bis (4-hydroxyaryl) oxindole (= isatin bisphenol), 5-chloruisatin, 5,7-dichloroisatin, 5-bromoisatin, etc. May be used as a part of the aromatic dihydroxy compound, and the amount used thereof may be And from 0.01 to 10 mol% against, and preferably 0.1 to 2 mol%.

  In the polymerization by the transesterification method, a carbonic acid diester is used as a monomer instead of phosgene. Representative examples of the carbonic acid diester include substituted diaryl carbonates typified by diphenyl carbonate and ditolyl carbonate, and dialkyl carbonates typified by dimethyl carbonate, diethyl carbonate, di-tert-butyl carbonate and the like. These carbonic acid diesters can be used alone or in admixture of two or more. Among these, diphenyl carbonate (hereinafter sometimes abbreviated as “DPC”) and substituted diphenyl carbonate are preferable.

  Moreover, said carbonic acid diester may substitute the quantity of the 50 mol% or less preferably 30 mol% or less with the dicarboxylic acid or dicarboxylic acid ester preferably. Representative dicarboxylic acids or dicarboxylic acid esters include terephthalic acid, isophthalic acid, diphenyl terephthalate, and diphenyl isophthalate. When substituted with such a dicarboxylic acid or dicarboxylic acid ester, a polyester carbonate is obtained.

  When an aromatic polycarbonate is produced by a transesterification method, a catalyst is usually used. Although there is no limitation on the catalyst species, generally basic compounds such as alkali metal compounds, alkaline earth metal compounds, basic boron compounds, basic phosphorus compounds, basic ammonium compounds, and amine compounds are used. Of these, alkali metal compounds and / or alkaline earth metal compounds are particularly preferred. These may be used alone or in combination of two or more. In the transesterification method, the polymerization catalyst is generally deactivated with p-toluenesulfonic acid ester or the like.

  Preferred aromatic polycarbonate resins are polycarbonate resins derived from 2,2-bis (4-hydroxyphenyl) propane or derived from 2,2-bis (4-hydroxyphenyl) propane and other aromatic dihydroxy compounds. And polycarbonate copolymers. Further, for the purpose of imparting flame retardancy and the like, a polymer or oligomer having a siloxane structure can be copolymerized. The aromatic polycarbonate resin may be a mixture of two or more polymers and / or copolymers of different raw materials, and may have a branched structure up to 0.5 mol%.

  The terminal hydroxyl group content of the polycarbonate resin has a great influence on the thermal stability, hydrolysis stability, color tone and the like of the molded product. In order to give practical physical properties, it is usually 30 to 2000 ppm, preferably 100 to 1500 ppm, more preferably 200 to 1000 ppm, and p-tert-butylphenol is used as a sealing end agent for adjusting the terminal hydroxyl group content. , Phenol, cumylphenol, p-long chain alkyl-substituted phenol, and the like can be used.

  As the amount of residual monomer in the polycarbonate resin, the aromatic dihydroxy compound is 150 ppm or less, preferably 100 ppm or less, and more preferably 50 ppm or less. When synthesized by the transesterification method, the residual amount of carbonic acid diester is 300 ppm or less, preferably 200 ppm or less, more preferably 150 ppm or less.

  The molecular weight of the polycarbonate resin is not particularly limited, but is a viscosity average molecular weight converted from the solution viscosity measured at a temperature of 20 ° C. using methylene chloride as a solvent, and preferably in the range of 10,000 to 50,000. More preferably, it is a thing of 11,000-40,000, Most preferably, it is a thing of the range of 12,000-30,000. By setting the viscosity average molecular weight to 10,000 or more, the mechanical properties are more effectively exhibited, and by setting the viscosity average molecular weight to 50,000 or less, the molding process becomes easier. Further, two or more kinds of polycarbonate resins having different viscosity average molecular weights may be mixed, or a polycarbonate resin having a viscosity average molecular weight outside the above preferred range may be mixed to be within the above molecular weight range.

[Polyethylene terephthalate resin]
The polyethylene terephthalate resin used in the present invention is a ratio of oxyethylene oxyterephthaloyl units (hereinafter sometimes referred to as “ET units”) composed of terephthalic acid and ethylene glycol to all the structural repeating units (hereinafter referred to as “ET ratio”). Is preferably a polyethylene terephthalate resin that is 90 equivalent% or more, and the polyethylene terephthalate resin in the present invention may contain constituent repeating units other than ET units in a range of less than 10 equivalent%. . The polyethylene terephthalate resin in the present invention is produced using terephthalic acid or a lower alkyl ester thereof and ethylene glycol as main raw materials, but other acid components and / or other glycol components may be used together as raw materials.

  Acid components other than terephthalic acid include phthalic acid, isophthalic acid, naphthalenedicarboxylic acid, 4,4'-diphenylsulfone dicarboxylic acid, 4,4'-biphenyldicarboxylic acid, 1,4-cyclohexanedicarboxylic acid, 1,3- Examples thereof include phenylenedioxydiacetic acid and structural isomers thereof, dicarboxylic acids such as malonic acid, succinic acid and adipic acid and derivatives thereof, and oxyacids such as p-hydroxybenzoic acid and glycolic acid or derivatives thereof.

  Examples of diol components other than ethylene glycol include 1,2-propanediol, 1,3-propanediol, 1,4-butanediol, aliphatic glycols such as pentamethylene glycol, hexamethylene glycol, and neopentyl glycol, cyclohexane Examples include alicyclic glycols such as dimethanol, and aromatic dihydroxy compound derivatives such as bisphenol A and bisphenol S.

  The raw material containing terephthalic acid or an ester-forming derivative thereof and ethylene glycol as described above is subjected to esterification or transesterification in the presence of an esterification catalyst or transesterification catalyst, and bis (β-hydroxyethyl) terephthalate and Then, an oligomer thereof is formed, and then a melt polycondensation is performed under high temperature and reduced pressure in the presence of a polycondensation catalyst and a stabilizer to obtain a polymer.

  The esterification catalyst is not particularly required because terephthalic acid serves as an autocatalyst for the esterification reaction. The esterification reaction can be carried out in the presence of an esterification catalyst and a polycondensation catalyst described later, and can be carried out in the presence of a small amount of an inorganic acid or the like. As the transesterification catalyst, alkali metal salts such as sodium and lithium, alkaline earth metal salts such as magnesium and calcium, and metal compounds such as zinc and manganese are preferably used. Above all, on the appearance of the obtained polyethylene terephthalate resin, Manganese compounds are particularly preferred.

  As the polycondensation catalyst, compounds soluble in a reaction system such as a germanium compound, an antimony compound, a titanium compound, a cobalt compound, and a tin compound are used alone or in combination. As the polycondensation catalyst, germanium dioxide is particularly preferable from the viewpoints of color tone and transparency. These polycondensation catalysts may be used in combination with a stabilizer in order to suppress the decomposition reaction during polymerization. Examples of the stabilizer include phosphate esters such as trimethyl phosphate, triethyl phosphate and triphenyl phosphate, and triphenyl phosphate. Phosphites such as phyto, trisdodecyl phosphite, methyl acid phosphate, dibutyl phosphate, monobutyl phosphate acidic phosphate, phosphorous compounds such as phosphoric acid, phosphorous acid, hypophosphorous acid, polyphosphoric acid Or 2 or more types are preferable.

  The use ratio of the above catalyst is usually in the range of 1 to 2000 ppm, preferably 3 to 500 ppm as the weight of the metal in the catalyst in the total polymerization raw material, and the use ratio of the stabilizer is the stabilizer in the total polymerization raw material. The weight of the phosphorus atom is usually 10 to 1000 ppm, preferably 20 to 200 ppm. The catalyst and the stabilizer can be supplied at any stage of the esterification reaction or transesterification reaction in addition to the preparation of the raw slurry. Further, it can be supplied at the beginning of the polycondensation reaction step.

The reaction temperature during the esterification reaction or transesterification reaction is usually 240 to 280 ° C., and the reaction pressure is usually 0.2 to 3 kg / cm ² G (20 to 300 kPa) as a relative pressure to the atmosphere. The reaction temperature during polycondensation is usually 250 to 300 ° C., and the reaction pressure is usually 500 to 0.1 mmHg (67 to 0.013 kPa) as an absolute pressure. Such esterification or transesterification reaction and polycondensation reaction may be performed in one step or in multiple steps. The polyethylene terephthalate resin thus obtained has an intrinsic viscosity of usually 0.45 to 0.70 dl / g, and is chipped by a conventional method. The average particle diameter of this chip is usually in the range of 2.0 to 5.5 mm, preferably 2.2 to 4.0 mm.

  Next, the polymer obtained by melt polycondensation as described above is usually subjected to solid phase polymerization. A polymer chip subjected to solid phase polymerization may be subjected to solid phase polymerization after preliminarily crystallizing by heating to a temperature lower than the temperature at which solid phase polymerization is performed in advance. Such precrystallization includes (a) a method in which a dry polymer chip is heated at a temperature of usually 120 to 200 ° C., preferably 130 to 180 ° C. for 1 minute to 4 hours, and (b) a dry polymer chip. A method of heating the water in an atmosphere of water vapor or water vapor-containing inert gas at a temperature of usually 120 to 200 ° C. for 1 minute or longer, (c) a polymer chip that absorbs moisture in a water, water vapor or water vapor-containing inert gas atmosphere and adjusts the humidity Can be performed by a method of heating at a temperature of usually 120 to 200 ° C. for 1 minute or more. The humidity control of the polymer chip is carried out so that the moisture content is usually in the range of 100 to 10,000 ppm, preferably 1000 to 5000 ppm. By subjecting the conditioned polymer chip to crystallization or solid phase polymerization, it is possible to further reduce the amount of acetaldehyde contained in PET and impurities contained in a trace amount.

The solid phase polymerization step consists of at least one stage, and usually has a polymerization temperature of 190 to 230 ° C., preferably 195 to 225 ° C., usually 1 kg / cm ² G to 10 mmHg (absolute pressure 200 to 1.3 kPa), preferably 0. The reaction is carried out under a flow of inert gas such as nitrogen, argon, carbon dioxide or the like under conditions of a polymerization pressure of 5 kg / cm ² G to 100 mmHg (150 to 13 kPa as an absolute pressure). The solid phase polymerization time may be shorter as the temperature is higher, but is usually 1 to 50 hours, preferably 5 to 30 hours, and more preferably 10 to 25 hours. The intrinsic viscosity of the polymer obtained by solid phase polymerization is usually in the range of 0.70 to 0.90 dl / g.

  The intrinsic viscosity of the polyethylene terephthalate resin used in the present invention may be appropriately selected and determined, but is usually 0.5 to 2 dl / g, particularly 0.6 to 1.5 dl / g, particularly 0.7 to 1. It is preferably 0 dl / g. By setting the intrinsic viscosity to 0.5 dl / g or more, particularly 0.7 dl / g or more, the mechanical properties, residence heat stability, chemical resistance, and heat-and-moisture resistance tend to be improved in the resin composition of the present invention. And preferred. On the other hand, the intrinsic viscosity is preferably less than 2 dl / g, particularly less than 1.0 dl / g, which tends to improve the fluidity of the resin composition.

  In the present invention, the intrinsic viscosity of the polyethylene terephthalate resin is a value measured at 30 ° C. using a mixed solvent of phenol / tetrachloroethane (weight ratio 1/1).

  The density | concentration of the terminal carboxyl group of the polyethylene terephthalate resin used for this invention is 1-60microeq / g normally, and it is preferable that it is 3-50microeq / g especially 5-40microeq / g. When the terminal carboxyl group concentration is 60 μeq / g or less, the mechanical properties of the resin composition tend to be improved. Conversely, when the terminal carboxyl group concentration is 1 μeq / g or more, the heat resistance of the resin composition is increased. It is preferable because the thermal stability and hue tend to be improved.

  The terminal carboxyl group concentration of the polyethylene terephthalate resin can be determined by dissolving 0.5 g of polyethylene terephthalate resin in 25 mL of benzyl alcohol and titrating with a 0.01 mol / L benzyl alcohol solution of sodium hydroxide. it can.

  The polyethylene terephthalate resin used in the present invention is obtained by subjecting the above-described polyethylene terephthalate resin to a polycondensation catalyst deactivation treatment. There is no restriction | limiting in particular as a deactivation processing method of the polycondensation catalyst of a polyethylene terephthalate resin, A conventionally well-known deactivation process can be given according to the polycondensation catalyst used. Examples of the deactivation treatment method include the following methods.

Deactivation treatment method of polycondensation catalyst 1: Hot water (steam) treatment of germanium catalyst A method of deactivating the germanium catalyst in the polyethylene terephthalate resin by treating the polyethylene terephthalate resin with hot water (steam).
Specifically, the container is filled with polyethylene terephthalate resin, and steam of 70 to 150 ° C., for example, about 100 ° C. is steamed in an amount of 1 to 100% by weight per hour for 5 to 6000 minutes with respect to the polyethylene terephthalate resin. Dry after treatment.
The polyethylene terephthalate resin is immersed in distilled water 0.3 to 10 times the weight of the polyethylene terephthalate resin in the container, and then the container containing the polyethylene terephthalate resin and distilled water is heated from the outside, and the internal temperature is set to 70 to 110. The temperature is controlled at 3 ° C. and the mixture is kept for 3 to 3000 minutes for hot water treatment, then dehydrated and dried.
The said drying is normally performed for 3 to 8 hours at 120-180 degreeC in inert gas, such as nitrogen.

Deactivation treatment method 2 of polycondensation catalyst: Addition of phosphorus compound to titanium catalyst A phosphorus compound is added to a polyethylene terephthalate resin to deactivate the titanium catalyst in the polyethylene terephthalate resin. In this case, the amount of phosphorus atoms added is preferably in the range of 7 to 145 ppm based on the weight of the polyethylene terephthalate resin. When the addition amount of the phosphorus compound is less than 7 ppm, the deactivation of the catalyst is insufficient, and the intended effect of the present invention may not be obtained. When the addition amount of phosphorus atoms exceeds 145 ppm, the phosphorus compound itself becomes coarse aggregated particles, causing problems such as poor appearance and reduced impact resistance.

  In addition, as a phosphorus compound to add, conventionally well-known phosphate ester compounds, phosphite ester compounds, phosphonate compounds, etc. are mentioned. Among these, phosphonate compounds represented by the following general formula (2) are preferable.

R ¹ OC (O) XP (O) (OR ² ) ₂ (2)
Wherein R ¹ and R ² are alkyl groups having 1 to 4 carbon atoms, X is —CH ₂ — or —CH (Y) — (Y represents a phenyl group), and R ¹ and R ² are Each may be the same or different.)

  Among the phosphonate compounds represented by the above formula (2), alkyl phosphonate compounds are preferably exemplified, and among these, triethylphosphonoacetic acid is particularly preferable. These may be used alone or in combination of two or more.

  The deactivation treatment method of the polycondensation catalyst of the polyethylene terephthalate resin is an example of a deactivation treatment that can be adopted in the present invention, and the deactivation treatment according to the present invention is not limited to the above method.

  Hereinafter, the polyethylene terephthalate resin subjected to the deactivation treatment of the polycondensation catalyst is referred to as “deactivated PET”, and the untreated polyethylene terephthalate resin is referred to as “untreated PET”.

The deactivated PET used in the present invention is such that the polycondensation catalyst in the polyethylene terephthalate resin is deactivated as described above, so that the solid phase polymerization rate Ks calculated by the following formula (1) is 0.006 ( dl / g · hr) or less, particularly 0.005 (dl / g · hr) or less, and particularly about 0.001 to 0.004 (dl / g · hr) is preferable.
Solid-phase polymerization rate Ks = ([η] s− [η] m) / T (1)
Here, [η] s is the intrinsic viscosity (dl / g) of the polyethylene terephthalate resin after the polyethylene terephthalate resin is held at 210 ° C. for 3 hours under a nitrogen stream, and [η] m is the polyethylene terephthalate. It is the intrinsic viscosity (dl / g) of the polyethylene terephthalate resin after holding the resin at 210 ° C. for 2 hours under a nitrogen stream. T is 1 (hour). That is, in the present invention, the intrinsic viscosity after holding at 210 ° C. for 3 hours under a nitrogen stream is [η] s, and the intrinsic viscosity after holding for 2 hours under the same conditions is [η] m. The solid phase polymerization rate Ks calculated by the above-described equation (1) was used as the solid phase polymerization rate Ks. T is 1 hour.

  When the solid phase polymerization rate Ks of the deactivated PET exceeds 0.006 (dl / g · hr), the deactivation treatment of the polycondensation catalyst is insufficient, and the effect of suppressing the residence heat deterioration according to the present invention is sufficiently obtained. Can't get. However, it is difficult to make the solid phase polymerization rate Ks excessively small, and it is usually 0.001 (dl / g · hr) or more.

[Resin component]
The resin component which concerns on this invention consists of 95-30 mass% of 1 type or 2 types or more of the above-mentioned polycarbonate resin, and 5-70 mass% of 1 type or 2 types or more of the above-mentioned deactivated PET.

  If the proportion of polycarbonate resin in the resin component is greater than the above upper limit and the proportion of deactivated PET is less than the above lower limit, the effect of improving chemical resistance by using PET cannot be sufficiently obtained, and conversely If the proportion of the polycarbonate resin is less than the above lower limit and the proportion of the deactivated PET is larger than the above upper limit, the original properties of the polycarbonate resin are impaired, and the impact resistance, heat resistance, etc. are lowered, which is not preferable.

  A preferable ratio is polycarbonate resin 90-40 mass%, deactivated PET 10-60 mass%, More preferably, polycarbonate resin 85-60 mass% and deactivated PET 15-40 mass%.

[Thermal stabilizer]
The resin composition of the present invention is required to contain a phosphorus-based heat stabilizer and / or a hindered phenol-based heat stabilizer with respect to the resin component described above, and by including these specific heat stabilizers, polyethylene By using deactivated PET as the terephthalate resin, the effect of suppressing residence heat deterioration can be further remarkably enhanced, and a resin composition having excellent resistance to residence heat deterioration can be realized. That is, the thermal degradation can be suppressed by the phosphorus thermal stabilizer by the decomposition of the peroxide and the hindered phenol thermal stabilizer by capturing the peroxide radical.

  Examples of phosphorus heat stabilizers include phosphorus heat stabilizers such as phosphites and phosphates.

  Examples of phosphites include triphenyl phosphite, trisnonylphenyl phosphite, tris (2,4-di-tert-butylphenyl) phosphite, trinonyl phosphite, tridecyl phosphite, and trioctyl phosphite. , Trioctadecyl phosphite, distearyl pentaerythritol diphosphite, tricyclohexyl phosphite, monobutyl diphenyl phosphite, monooctyl diphenyl phosphite, distearyl pentaerythritol diphosphite, bis (2,4-di-tert-butyl Phenyl) pentaerythritol phosphite, bis (2,6-di-tert-butyl-4-methylphenyl) pentaerythritol phosphite, 2,2-methylenebis (4,6-di-tert) Butylphenyl) triesters of phosphorous acid such as octyl phosphite, diesters, monoesters, and the like.

  Examples of phosphate esters include trimethyl phosphate, triethyl phosphate, tributyl phosphate, trioctyl phosphate, triphenyl phosphate, tricresyl phosphate, tris (nonylphenyl) phosphate, 2-ethylphenyl diphenyl phosphate, tetrakis (2,4-di-). tert-butylphenyl) -4,4-diphenylphosphonite and the like.

  Among the above phosphorus-based heat stabilizers, distearyl pentaerythritol diphosphite, bis (2,4-di-tert-butylphenyl) pentaerythritol phosphite, bis (2,6-di-tert-butyl-4) -Methylphenyl) pentaerythritol phosphite, phosphite compounds such as tris (2,4-di-tert-butylphenyl) phosphite are preferred, and among them bis (2,6-di-tert-butyl-4-methylphenyl) Pentaerythritol phosphite and tris (2,4-di-t-butylphenyl) phosphite are particularly preferred.

  As the hindered phenol heat stabilizer, pentaerythritol tetrakis [3- (3,5-di-tert-butyl-4-hydroxyphenyl) propionate], octadecyl-3- (3,5-di-tert-butyl- 4-hydroxyphenyl) propionate, thiodiethylenebis [3- (3,5-di-tert-butyl-4-hydroxyphenyl) propionate], N, N′-hexane-1,6-diylbis [3- (3 5-di-tert-butyl-4-hydroxyphenylpropionamide), 2,4-dimethyl-6- (1-methylpentadecyl) phenol, diethyl [[3,5-bis (1,1-dimethylethyl)- 4-hydroxyphenyl] methyl] phosphoate, 3,3 ′, 3 ″, 5,5 ′, 5 ″ -hexa-tert Butyl-a, a ′, a ″-(mesitylene-2,4,6-triyl) tri-p-cresol, 4,6-bis (octylthiomethyl) -o-cresol, ethylenebis (oxyethylene) bis [3- (5-tert-butyl-4-hydroxy-m-tolyl) propionate], hexamethylenebis [3- (3,5-di-tert-butyl-4-hydroxyphenyl) propionate], 1,3 5-tris (3,5-di-tert-butyl-4-hydroxybenzyl) -1,3,5-triazine-2,4,6 (1H, 3H, 5H) -trione, 2,6-di-tert -Butyl-4- (4,6-bis (octylthio) -1,3,5-triazin-2-ylamino) phenol and the like.

  Among the above, pentaerythritol tetrakis [3- (3,5-di-tert-butyl-4-hydroxyphenyl) propionate], octadecyl-3- (3,5-di-tert-butyl-4-hydroxyphenyl) Propionate is preferred. These two phenolic heat stabilizers are commercially available from Ciba Specialty Chemicals under the names “Irganox 1010” and “Irganox 1076”.

  A phosphorus heat stabilizer may be used individually by 1 type, and may use 2 or more types together. Moreover, about a hindered phenol-type heat stabilizer, 1 type may be used independently and 2 or more types may be used together. Moreover, you may use together a phosphorus thermal stabilizer and a hindered phenol thermal stabilizer.

  The phosphorus-based heat stabilizer is used in an amount of 0.01 to 0.5 parts by weight, preferably 0.02 to 0.2 parts by weight, based on 100 parts by weight of the resin component composed of polycarbonate resin and deactivated PET. The hindered phenol heat stabilizer is used in an amount of 0.01 to 1 part by mass, preferably 0.05 to 0.2 part by mass, based on 100 parts by mass of the resin component composed of polycarbonate resin and deactivated PET. If the blending amount of these heat stabilizers is too small, it is not possible to sufficiently obtain the effect of suppressing the thermal deterioration due to the blending of the heat stabilizer, and if it is too much, the effect reaches a peak and is not economical. In addition, when using together a phosphorus heat stabilizer and a hindered phenol heat stabilizer, after making each heat stabilizer into the said mixing | blending range, a total compounding ratio is polycarbonate resin, deactivated PET resin, and It is preferable to use it so that it may become 0.07-0.4 mass part with respect to 100 mass parts of resin components which consist of.

[Elastomer]
The PC / PET composite resin composition of the present invention contains 1 to 10 parts by weight of an elastomer and 1 to 20 parts by weight of an inorganic filler with respect to 100 parts by weight of a resin component comprising a polycarbonate resin and deactivated PET. One of the characteristics is to suppress the thickening of the resin composition during heat retention by blending a specific amount of elastomer. That is, by using an elastomer amount, and preferably a specific elastomer, the aggregation of the elastomer during heat retention is suppressed, and the thickening due to the aggregation of the elastomer is suppressed, whereby the molding stability of the polycarbonate resin composition is reduced. Can be improved.

  The elastomer used in the present invention is a rubbery polymer having a glass transition temperature of 0 ° C. or lower, in particular −20 ° C. or lower, or a copolymer obtained by copolymerizing a monomer component copolymerizable therewith. Any conventionally known compound that can be blended in a product or the like to improve its mechanical properties can be used.

  Examples of elastomers include polybutadiene, polyisoprene, diene copolymers (styrene / butadiene copolymers, acrylonitrile / butadiene copolymers, acrylic / butadiene rubbers, etc.), and copolymers of ethylene and α-olefin (ethylene).・ Propylene copolymers, ethylene / butene copolymers, ethylene / octene copolymers, etc., copolymers of ethylene and unsaturated carboxylic acid esters (ethylene / methacrylate copolymers, ethylene / butyl acrylate copolymers, etc.) ), Copolymers of ethylene and aliphatic vinyl compounds, terpolymers of ethylene, propylene and non-conjugated dienes, acrylic rubber (polybutyl acrylate, poly (2-ethylhexyl acrylate), butyl acrylate / 2-ethylhexyl acrylate copolymer Union) Corn-based rubber (a polyorganosiloxane rubber; polyorganosiloxane rubber and a polyalkyl (meth) consisting of acrylate rubber-IPN composite rubber etc.) and the like. These may be used alone or in combination of two or more. “(Meth) acrylate” means “acrylate” and “methacrylate”, and “(meth) acrylic acid” described later means “acrylic acid” and “methacrylic acid”.

  Preferred examples of the monomer component copolymerized with such an elastomer include aromatic vinyl compounds, vinyl cyanide compounds, (meth) acrylic acid ester compounds, (meth) acrylic acid compounds, and the like. Other monomer components include epoxy group-containing (meth) acrylic acid ester compounds such as glycidyl (meth) acrylate; maleimide compounds such as maleimide, N-methylmaleimide, N-phenylmaleimide; maleic acid, phthalic acid, itacon Examples thereof include α, β-unsaturated carboxylic acid compounds such as acids and anhydrides thereof, such as maleic anhydride. These monomer components may be used alone or in combination of two or more.

  In order to improve the molding stability of the resin composition of the present invention, it is particularly preferable to use a core / shell type graft copolymer type elastomer as the elastomer. In particular, at least one rubber polymer selected from butadiene-containing rubber, butyl acrylate-containing rubber, 2-ethylhexyl acrylate-containing rubber, and silicone-based rubber is used as a core layer, and an acrylic ester, a methacrylic ester, and a fragrance around the core layer. A core / shell type graft copolymer comprising a shell layer formed by copolymerizing at least one monomer component selected from an aromatic vinyl compound is particularly preferred. More specifically, methyl methacrylate-butadiene-styrene polymer (MBS), methyl methacrylate-acrylonitrile-butadiene-styrene polymer (MABS), methyl methacrylate-butadiene polymer (MB), methyl methacrylate-acrylic rubber polymer ( MA), methyl methacrylate-acrylic butadiene rubber copolymer, methyl methacrylate-acrylic butadiene rubber-styrene copolymer, methyl methacrylate- (acrylic silicone IPN (interpenetrating polymer network) rubber) polymer, etc. Mention may be made of a core / shell type elastomer comprising a polymethyl methacrylate (PMMA) -based polymerization or copolymer block.

  Examples of such core / shell type elastomers include the EXL series such as Paraloid EXL2315, EXL2602, and EXL2603 manufactured by Rohm & Haas Japan, the KM series such as KM330 and KM336P, the KCZ series such as KCZ201, and the Mitsubishi Rayon. Examples include Metablene S-2001 and SRK-200 manufactured by the company.

  Other specific examples of the rubbery polymer obtained by copolymerizing a rubbery polymer with a monomer component copolymerizable therewith include polybutadiene rubber, styrene-butadiene copolymer (SBR), and styrene-butadiene-styrene. Block copolymer (SBS), styrene-ethylene / butylene-styrene block copolymer (SEBS), styrene-ethylene / propylene-styrene block copolymer (SEPS), ethylene-ethyl acrylate copolymer (EEA), ethylene -A methyl acrylate copolymer (EMA) etc. are mentioned.

  These elastomers may be used individually by 1 type, and may use 2 or more types together.

The content ratio of the elastomer in the PC / PET composite resin composition of the present invention is 1 to 10 parts by mass, preferably 2 to 9 parts by mass, more preferably 100 parts by mass of the resin component composed of polycarbonate resin and deactivated PET. Is 3-8 parts by mass.
If the elastomer content is less than the above lower value, the impact strength improvement effect and the molding stability improvement effect due to the blending of the elastomer cannot be sufficiently obtained, and if the upper limit value is exceeded, the thermal stability and rigidity are inferior. There is a case.

[Inorganic filler]
The PC / PET composite resin composition of the present invention contains 1 to 10 parts by mass of an elastomer and 1 to 20 parts by mass of an inorganic filler with respect to 100 parts by mass of a resin component composed of a polycarbonate resin and deactivated PET. One of the characteristics is to suppress the thickening of the resin composition during heat retention by blending a specific amount of inorganic filler. Further, as the inorganic filler used in the present invention, by using a surface treatment that has been improved in adhesion with the resin component, poor dispersion of the inorganic filler during heat retention is suppressed, resulting in aggregation. It is more preferable because it can suppress thickening and improve the molding stability of the polycarbonate resin composition.

  Examples of the inorganic filler used in the present invention include glass fiber, carbon fiber, metal fiber, ceramic fiber, milled fiber thereof, slag fiber, rock wool, wollastonite, zonotlite, potassium titanate whisker, aluminum borate. Fibrous inorganic fillers such as whiskers, boron whiskers, basic magnesium sulfate whiskers, silicate compounds such as glass flakes, glass beads, graphite, talc, mica, kaolinite, sepiolite, attapulgite, montmorillonite, bentonite, smectite, silica And inorganic fillers such as alumina and calcium carbonate. These inorganic fillers may have a surface coated with a different material such as metal-coated glass fiber or metal-coated carbon fiber. These inorganic fillers may be used alone or in combination of two or more.

  Among these, glass fiber, carbon fiber, and these milled fibers are advantageous in terms of improving molding stability. In particular, the glass fiber and the milled fiber are stronger than the resin component composed of polycarbonate resin and deactivated PET. This is advantageous in that good adhesion is achieved. As the inorganic filler used in the present invention, glass fiber is particularly preferable.

As glass fiber, glass compositions, such as A glass, C glass, and E glass, are not specifically limited, In some cases, components such as TiO ₂ , SO ₃ , and P ₂ O ₅ may be contained. However, E glass (non-alkali glass) is more preferable.

  Moreover, although it does not specifically limit as an average fiber diameter of glass fiber, A 1-25 micrometers thing is used normally, Preferably it is 3-17 micrometers. Glass fibers having an average fiber diameter in this range are good in terms of both the thermal expansion coefficient and the resistance to peeling force. When the fiber diameter is reduced, the area of the interface with the resin component is increased, so that the effect of improving the molding stability is good. However, the unfavorable influence on the peeling force by the interface increases. Where interfacial adhesion is a priority, the use of larger diameter glass fibers can be a prescription.

  The preferred fiber length of the glass fiber is 50 to 1,000 μm, preferably 100 to 500 μm, particularly preferably 120 to 300 μm, as the number average fiber length in the resin composition pellet or molded product. The number average fiber length of the glass fibers is calculated by an image analysis device from an optical microscope observation or the like from a residue of glass fibers collected after dissolving a molded product in a solvent or decomposing a resin with a basic compound. Value. In calculating the number average fiber length, fibers having a length equal to or less than the fiber diameter are not counted. In other fibrous fillers, the number average fiber length is suitably 1,000 μm or less.

  The inorganic filler such as glass fiber is preferably surface-treated with a silane coupling agent or the like in order to achieve stronger adhesion between the polycarbonate resin and the resin component made of deactivated PET. Examples of reactive groups in such silane coupling agents include epoxy groups, amino groups, vinyl groups, and methacryloxy groups, with epoxy groups and amino groups being particularly preferred.

  Further, glass fibers and carbon fibers are usually coated with a surface for bundling the fibers. Since the adhesiveness with the resin component is greatly influenced by the surface coating agent, the selection of the surface coating agent is important. A surface coating agent composed of an epoxy group-containing compound is preferred from the viewpoint of securing a strong bond with the resin component and improving molding stability. The epoxy group-containing compound is rich in reactivity with a resin component composed of a polycarbonate resin and deactivated PET, has good adhesion, and is excellent in adhesion moisture and heat resistance.

  Although various epoxy group-containing compounds can be used as the surface treatment agent for inorganic fillers such as glass fibers, the epoxy group-containing compound preferably has a polymer structure having a molecular weight of 500 or more. Preferably, it contains a plurality of epoxy groups in one molecule. Moreover, the structure mainly comprised from an aromatic ring from a heat resistant viewpoint is preferable.

  More specifically, suitable epoxy group-containing compounds include epoxy resins, especially phenol novolac type epoxy resins and linear cresol novolac type epoxy resins, with phenol novolac type epoxy resins being particularly preferred.

  In the present invention, the glass fiber preferably used as an inorganic filler has a glycidyl group on the surface by being treated with the above-described silane coupling agent having an epoxy group or a surface coating agent comprising an epoxy group-containing compound. It is preferable in that the effect of the present invention becomes remarkable.

The content ratio of the inorganic filler in the PC / PET composite resin composition of the present invention is 1 to 20 parts by mass, preferably 2 to 15 parts by mass, with respect to 100 parts by mass of the resin component composed of polycarbonate resin and deactivated PET. More preferably, it is 3-10 mass parts.
If the content of the inorganic filler is less than the above lower limit, the effect of improving the dimensional stability and rigidity due to the blending of the inorganic filler cannot be obtained sufficiently, and if the upper limit is exceeded, the impact strength may be inferior. is there.

[Combination of elastomer and inorganic filler]
In the present invention, as described above, by using together 1 to 10 parts by mass of an elastomer and 1 to 20 parts by mass of an inorganic filler with respect to 100 parts by mass of a resin component made of polycarbonate resin and deactivated PET, molding stability In order to obtain the effect of improving the property more effectively, it is preferable to use the elastomer and the inorganic filler in a mass part ratio of elastomer: inorganic filler = 1: 0.1-20, particularly 1: 0.2-10. Moreover, it is preferable to use 2-30 mass parts with respect to 100 mass parts of resin components which consist of a polycarbonate resin and deactivated PET in total with an elastomer and an inorganic filler, and especially 5-20 mass parts.

[Other ingredients]
In the resin composition according to the present invention, the polycarbonate resin and the deactivated PET, the heat stabilizer, the elastomer, and the inorganic filler, as well as the ordinary polycarbonate resin composition, as long as the effects of the present invention are not impaired. It may contain other various additives.

  As various additives that can be contained, antioxidants, mold release agents, ultraviolet absorbers, dyes and pigments, reinforcing agents, flame retardants, impact resistance improvers, antistatic agents, antifogging agents, lubricants and antiblocking agents, Examples thereof include a fluidity improver, a plasticizer, a dispersant, and a fungicide. Two or more of these may be used in combination. Hereinafter, an example of an additive suitable for the resin composition of the present invention will be specifically described.

  The release agent includes at least one compound selected from the group consisting of aliphatic carboxylic acids, esters of aliphatic carboxylic acids and alcohols, aliphatic hydrocarbon compounds having a number average molecular weight of 200 to 15000, and polysiloxane silicone oil. Can be mentioned.

  Examples of the aliphatic carboxylic acid include saturated or unsaturated aliphatic monovalent, divalent or trivalent carboxylic acid. Here, the aliphatic carboxylic acid includes alicyclic carboxylic acid. Among these, preferable aliphatic carboxylic acids are monovalent or divalent carboxylic acids having 6 to 36 carbon atoms, and aliphatic saturated monovalent carboxylic acids having 6 to 36 carbon atoms are more preferable. Specific examples of such aliphatic carboxylic acids include palmitic acid, stearic acid, caproic acid, capric acid, lauric acid, arachidic acid, behenic acid, lignoceric acid, serotic acid, mellicic acid, tetrariacontanoic acid, montanic acid, adipine Examples include acids and azelaic acid.

  As the aliphatic carboxylic acid in the ester of an aliphatic carboxylic acid and an alcohol, the same one as the aliphatic carboxylic acid can be used. On the other hand, examples of the alcohol include saturated or unsaturated monovalent or polyhydric alcohols. These alcohols may have a substituent such as a fluorine atom or an aryl group. Among these, a monovalent or polyvalent saturated alcohol having 30 or less carbon atoms is preferable, and an aliphatic saturated monohydric alcohol or polyhydric alcohol having 30 or less carbon atoms is more preferable. Here, aliphatic includes alicyclic compounds. Specific examples of such alcohols include octanol, decanol, dodecanol, stearyl alcohol, behenyl alcohol, ethylene glycol, diethylene glycol, glycerin, pentaerythritol, 2,2-dihydroxyperfluoropropanol, neopentylene glycol, ditrimethylolpropane, dipentaerythritol and the like. Is mentioned.

  In addition, said ester compound may contain aliphatic carboxylic acid and / or alcohol as an impurity, and may be a mixture of a some compound.

  Specific examples of esters of aliphatic carboxylic acids and alcohols include beeswax (a mixture based on myricyl palmitate), stearyl stearate, behenyl behenate, stearyl behenate, glycerin monopalmitate, glycerin monostearate Examples thereof include rate, glycerol distearate, glycerol tristearate, pentaerythritol monopalmitate, pentaerythritol monostearate, pentaerythritol distearate, pentaerythritol tristearate, pentaerythritol tetrastearate and the like.

  Examples of the aliphatic hydrocarbon having a number average molecular weight of 200 to 15000 include liquid paraffin, paraffin wax, microwax, polyethylene wax, Fischer-Tropsch wax, and α-olefin oligomer having 3 to 12 carbon atoms. Here, as the aliphatic hydrocarbon, alicyclic hydrocarbon is also included. Moreover, these hydrocarbon compounds may be partially oxidized. Among these, paraffin wax, polyethylene wax, or a partial oxide of polyethylene wax is preferable, and paraffin wax and polyethylene wax are more preferable. The number average molecular weight is preferably 200 to 5,000. These aliphatic hydrocarbons may be a single substance, or may be a mixture of various constituent components and molecular weights, as long as the main component is within the above range.

  Examples of the polysiloxane silicone oil include dimethyl silicone oil, phenylmethyl silicone oil, diphenyl silicone oil, and fluorinated alkyl silicone. Two or more of these may be used in combination.

  Content of a mold release agent is 0.001-2 mass parts normally with respect to a total of 100 mass parts of polycarbonate resin and deactivated PET, Preferably it is 0.01-1 mass part. When the content of the release agent is less than 0.001 part by mass, the effect of releasability may not be sufficient. When the content exceeds 2 parts by mass, the hydrolysis resistance is deteriorated and the mold is contaminated during injection molding. There are problems such as.

  Specific examples of the ultraviolet absorber include organic ultraviolet absorbers such as benzotriazole compounds, benzophenone compounds, and triazine compounds in addition to inorganic ultraviolet absorbers such as cerium oxide and zinc oxide. Of these, organic ultraviolet absorbers are preferred. In particular, benzotriazole compounds, 2- (4,6-diphenyl-1,3,5-triazin-2-yl) -5-[(hexyl) oxy] -phenol, 2- [4,6-bis (2, 4-Dimethylphenyl) -1,3,5-triazin-2-yl] -5- (octyloxy) phenol, 2,2 ′-(1,4-phenylene) bis [4H-3,1-benzoxazine-4- ON], [(4-methoxyphenyl) -methylene] -propanedioic acid-dimethyl ester is preferred.

  Specific examples of the benzotriazole compound include condensates of methyl-3- [3-tert-butyl-5- (2H-benzotriazol-2-yl) -4-hydroxyphenyl] propionate-polyethylene glycol. Specific examples of other benzotriazole compounds include 2-bis (5-methyl-2-hydroxyphenyl) benzotriazole, 2- (3,5-di-tert-butyl-2-hydroxyphenyl) benzotriazole, 2- (3 ′, 5′-di-tert-butyl-2′-hydroxyphenyl) -5-chlorobenzotriazole, 2- (3-tert-butyl-5-methyl-2-hydroxyphenyl) -5-chloro Benzotriazole, 2- (2′-hydroxy-5′-tert-octylphenyl) benzotriazole, 2- (3,5-di-tert-amyl-2-hydroxyphenyl) benzotriazole, 2- [2-hydroxy- 3,5-bis (α, α-dimethylbenzyl) phenyl] -2H-benzotriazole, 2,2′-methyl Ren-bis [4- (1,1,3,3-tetramethylbutyl) -6- (2N-benzotriazol-2-yl) phenol] [methyl-3- [3-tert-butyl-5- (2H- Benzotriazol-2-yl) -4-hydroxyphenyl] propionate-polyethylene glycol] condensate. Two or more of these may be used in combination.

  Of the above, preferably 2- (2′-hydroxy-5′-tert-octylphenyl) benzotriazole, 2- [2-hydroxy-3,5-bis (α, α-dimethylbenzyl) phenyl]- 2H-benzotriazole, 2- (4,6-diphenyl-1,3,5-triazin-2-yl) -5-[(hexyl) oxy] -phenol, 2- [4,6-bis (2,4 -Dimethylphenyl) -1,3,5-triazin-2-yl] -5- (octyloxy) phenol, 2,2'-methylene-bis [4- (1,1,3,3-tetramethylbutyl)- 6- (2N-benzotriazol-2-yl) phenol].

  Content of a ultraviolet absorber is 0.01-3 mass parts normally with respect to a total of 100 mass parts of polycarbonate resin and deactivated PET, Preferably it is 0.1-1 mass part. When the content of the ultraviolet absorber is less than 0.01 parts by mass, the effect of improving the weather resistance may be insufficient, and when it exceeds 3 parts by mass, a problem such as mold deposit may occur.

  Examples of the dye / pigment include inorganic pigments, organic pigments, and organic dyes. Examples of inorganic pigments include, for example, sulfide pigments such as carbon black, cadmium red, and cadmium yellow; silicate pigments such as ultramarine blue; zinc white, petal, chromium oxide, titanium oxide, iron black, titanium yellow, and zinc- Oxide pigments such as iron brown, titanium cobalt green, cobalt green, cobalt blue, copper-chromium black and copper-iron black; chromic pigments such as yellow lead and molybdate orange; Examples include Russian pigments. Organic pigments and organic dyes include phthalocyanine dyes such as copper phthalocyanine blue and copper phthalocyanine green; azo dyes such as nickel azo yellow; thioindigo, perinone, perylene, quinacridone, dioxazine, isoindolinone And condensed polycyclic dyes such as quinophthalone; anthraquinone, heterocyclic, and methyl dyes and the like. Two or more of these may be used in combination. Among these, carbon black, titanium oxide, cyanine-based, quinoline-based, anthraquinone-based, and phthalocyanine-based compounds are preferable from the viewpoint of thermal stability.

  The content of the dye / pigment is usually 5 parts by mass or less, preferably 3 parts by mass or less, and more preferably 2 parts by mass or less with respect to 100 parts by mass in total of the polycarbonate resin and deactivated PET. When the content of the dye / pigment exceeds 5 parts by mass, the impact resistance may not be sufficient.

  Examples of the flame retardant include halogenated bisphenol A polycarbonate, brominated bisphenol epoxy resin, brominated bisphenol phenoxy resin, halogenated flame retardant such as brominated polystyrene, phosphate ester flame retardant, diphenylsulfone-3,3 ′. -Organic metal salt flame retardants such as dipotassium disulfonate, potassium diphenylsulfone-3-sulfonate, potassium perfluorobutanesulfonate, and polyorganosiloxane flame retardants are preferable, but phosphate ester flame retardants are particularly preferable. .

  Specific examples of the phosphate ester flame retardant include triphenyl phosphate, resorcinol bis (dixylenyl phosphate), hydroquinone bis (dixylenyl phosphate), 4,4′-biphenol bis (dixylenyl phosphate), bisphenol A Examples thereof include bis (dixylenyl phosphate), resorcinol bis (diphenyl phosphate), hydroquinone bis (diphenyl phosphate), 4,4′-biphenol bis (diphenyl phosphate), bisphenol A bis (diphenyl phosphate), and the like. Two or more of these may be used in combination. In these, resorcinol bis (dixylenyl phosphate) and bisphenol A bis (diphenyl phosphate) are preferable.

  Content of a flame retardant is 1-30 mass parts normally with respect to a total of 100 mass parts of polycarbonate resin and deactivated PET, Preferably it is 3-25 mass parts, More preferably, it is 5-20 mass parts. When the content of the flame retardant is less than 1 part by mass, the flame retardancy may not be sufficient, and when it exceeds 30 parts by mass, the heat resistance may decrease.

  Examples of the anti-dripping agent include fluorinated polyolefins such as polyfluoroethylene, and polytetrafluoroethylene having fibril forming ability is particularly preferable. This shows the tendency to disperse | distribute easily in a polymer and to couple | bond together polymers and to make a fibrous material. Polytetrafluoroethylene having fibril-forming ability is classified as type 3 according to the ASTM standard. Polytetrafluoroethylene can be used in solid form or in the form of an aqueous dispersion. Examples of polytetrafluoroethylene having fibril-forming ability include “Teflon (registered trademark) 6J” or “Teflon (registered trademark) 30J” from Mitsui DuPont Fluorochemical Co., Ltd. and “Polyflon (trade name) from Daikin Industries, Ltd. Is commercially available.

  Content of a dripping inhibitor is 0.02-4 mass parts normally with respect to a total of 100 mass parts of polycarbonate resin and deactivated PET, Preferably it is 0.03-3 mass parts. When the compounding amount of the dripping inhibitor exceeds 5 parts by mass, the appearance of the molded product may be deteriorated.

  The resin composition according to the present invention may contain other resin components and rubber components other than the polycarbonate resin and the deactivated PET and the above-mentioned elastomer. In this case, as other resin or rubber component, for example, acrylonitrile-styrene copolymer, acrylonitrile-butadiene-styrene copolymer, styrene resin such as polystyrene resin, polyolefin resin such as polyethylene resin and polypropylene resin, polyamide resin , Polyimide resin, polyetherimide resin, polyurethane resin, polyphenylene ether resin, polyphenylene sulfide resin, polysulfone resin, polymethacrylate resin, phenol resin, epoxy resin, etc., but the content of these other resins or rubber components is In order to sufficiently secure the effect of the combined use of the polycarbonate resin and the deactivated PET, it is preferably 20 parts by mass or less with respect to 100 parts by mass in total of the polycarbonate resin and the deactivated PET.

[Method for producing PC / PET composite resin composition]
The PC / PET composite resin composition of the present invention is a polycarbonate resin, deactivated PET, elastomer, inorganic filler, phosphorus-based heat stabilizer and / or hindered phenol-based heat stabilizer, and others added as necessary. Using any of these additives, any conventionally known method can be appropriately selected for production.

  Specifically, polycarbonate resins, deactivated PET, elastomers, inorganic fillers, phosphorus-based heat stabilizers and / or hindered phenol-based heat stabilizers, and additives that are blended as necessary are added to tumblers and Henschel mixers. The resin composition can be produced by premixing using various mixers such as a banbury mixer, roll, brabender, single-screw kneading extruder, twin-screw kneading extruder, kneader and the like. Moreover, it is also possible to produce a resin composition without mixing each component in advance, or by mixing only some components in advance and supplying them to an extruder using a feeder and melt-kneading them.

[Preferable physical properties of PC / PET composite resin composition]
Of PC / PET composite resin composition of the present invention, preferred is a number average molecular weight Mn _x chloroform solubles was held 60 minutes at 280 ° C., chloroform-soluble before holding for 60 minutes at 280 ° C. retention to the number average molecular weight Mn _o minute, _i.e., the number average molecular weight of retention after heat retention calculated by Mn x / Mn _o × 100 is 80% or more. If the retention of this number average molecular weight is less than 80%, it cannot be said that the effect of suppressing the residence heat degradation intended in the present invention is sufficient, and there is a problem of residence heat degradation. Preferably, the number average molecular weight retention is 85% or more, more preferably 90% or more.

Also, of the PC / PET composite resin composition of the present invention, preferred are 280 Charpy impact strength Ip _x after holding for 60 minutes at ° C. is before the 60 minute hold at 280 ° C. Charpy impact strength Ip _o 80%, _i.e., retention of Charpy impact strength after heat retention calculated by Ip x / Ip _o × 100 is 80% or more. If the Charpy impact strength retention rate is less than 80%, it cannot be said that the effect of suppressing the residence heat deterioration intended in the present invention is sufficient, and there is a problem of residence heat degradation. Preferably, the Charpy impact strength retention is 85% or more, more preferably 90% or more.

Incidentally, the Charpy impact strength Ip _o of PC / PET composite resin composition of the present invention is 10.0 kJ / ^{m 2} or more, and particularly preferably 12.0kJ / ^{m 2} or more.

Further, among the PC / PET composite resin compositions of the present invention, the preferable one is that the resin composition is held at 280 ° C. for 30 minutes, and then the MFR of the molded product injection-molded is [R _x ], and the resin composition is When the MFR of a molded product injection-molded immediately after injection into the injection molding machine is [R _o ], the decrease rate of MFR [R _x ] with respect to MFR [R _o ] calculated by the following equation (3) is − It is a PC / PET composite resin composition characterized by being 20 to 20%.
Reduction rate of MFR = (R _o −R _x ) / R _o × 100 (3)

In the present invention, the resin composition is retained in a cylinder at a cylinder temperature of 280 ° C. for 30 minutes and then injection molded at the cylinder temperature (hereinafter simply referred to as “injection molding”). the MFR and [R _x], and then after the injection of the resin composition in a 280 ° C. of the cylinder, after a sufficient filling amount of injection molding, the MFR of the molded product thus obtained was immediately injection-molded [ R _o ], and using these values, the MFR reduction rate was calculated by the above-described equation (3). As an injection molding machine, “M150AII-SJ type” manufactured by Meiki Seisakusho was used.

  When the MFR reduction rate exceeds 20% or less than −20%, the flowability of the resin composition changes greatly with time in injection molding, making it difficult to perform injection molding under the same conditions. Molding defects such as occurrence occur. It is particularly preferable that the MFR reduction rate is -10 to 10%.

  In the present invention, the number average molecular weight, Charpy impact strength, and MFR of the PC / PET composite resin composition are values measured by the methods described in the Examples section below.

  In addition, the condition for maintaining the number average molecular weight and Charpy impact strength of the PC / PET composite resin composition described above as “280 ° C., 60 minutes (1 hour)” is the usual PC / PET composite resin. Assuming the highest temperature and the longest residence time of the cylinder in the injection molding of the composition, and 1 hour at 280 ° C., if there is no problem of residence heat deterioration of the resin composition, This is based on the assumption that the accumulated heat deterioration does not occur in normal use.

  On the other hand, the holding condition in the evaluation of the MFR reduction rate is “280 ° C., 30 minutes” because the increase in viscosity accompanying the aggregation of the elastomer and inorganic filler contained in the resin composition is caused in the molding machine. Occurs after about 15 to 30 minutes, and thereafter, the change in moldability tends to be apparently offset against the decrease in viscosity due to the decrease in the molecular weight of the polycarbonate resin, so that the most suitable residence time for evaluation is 30 minutes. This is because.

[Method for producing PC / PET composite resin molded product]
The method for producing a molded product from the PC / PET composite resin composition of the present invention is not particularly limited, and a molding method generally employed for thermoplastic resins, that is, a general injection molding method, an ultra-high-speed injection method. Molding method, injection compression molding method, multicolor injection molding method, gas assist injection molding method, molding method using heat insulation mold, molding method using rapid heating / cooling mold, foam molding (including supercritical fluid), Insert molding, IMC (in-mold coating molding) molding method, extrusion molding method, sheet molding method, thermoforming method, rotational molding method, laminate molding method, press molding method and the like can be employed. Also, in various injection molding methods, a molding method using a hot runner method can be selected.

  Further, the PC / PET composite resin composition of the present invention can be subjected to multicolor composite molding with another thermoplastic resin composition to form a composite molded product.

  In the present invention, deactivated PET is used as the polyethylene terephthalate resin, a specific heat stabilizer is blended, and a specific amount of elastomer and inorganic filler are used to compound the polyethylene terephthalate resin with the polycarbonate resin. Residual heat deterioration of the resin composition due to this is suppressed, so the problem of residence heat deterioration in the molding process is prevented, but if this residence temperature is too high and the residence time is too long, the residence heat deterioration May cause problems. Therefore, the residence temperature of the resin composition in the molding step of the PC / PET composite resin composition of the present invention is preferably 280 ° C. or less and the residence time is 60 minutes or less.

  Hereinafter, the present invention will be described more specifically with reference to examples and comparative examples. However, the present invention is not limited to these examples as long as the gist thereof is not exceeded.

  In addition, the compounding component of the resin composition used in the Example and the comparative example is as follows.

  Polycarbonate resin 1: Product from Mitsubishi Engineering Plastics Co., Ltd. Aromatic polycarbonate resin “Product name: Iupilon (registered trademark) S-3000”, viscosity average molecular weight 21,500, terminal hydroxyl group content 150 ppm

  Polycarbonate resin 2: Products manufactured by Mitsubishi Engineering Plastics Co., Ltd. Aromatic polycarbonate resin "Product name: Iupilon (registered trademark) S-3000" (viscosity average molecular weight 21,500, terminal hydroxyl group content 150 ppm) and Mitsubishi Engineering Plastics Products Co., Ltd. Aromatic polycarbonate resin "trade name: Iupilon (registered trademark) H-4000" (viscosity average molecular weight 16,000, terminal hydroxyl group content 100 ppm), a mixture, S-3000 / H-4000 = 81 / 19 (weight ratio), viscosity average molecular weight 20,500

  Polycarbonate resin 3: Products manufactured by Mitsubishi Engineering Plastics Co., Ltd. Aromatic polycarbonate resin "Product name: Iupilon (registered trademark) S-3000" (viscosity average molecular weight 21,500, terminal hydroxyl group content 150 ppm) and Mitsubishi Engineering Plastics Products Co., Ltd. Aromatic polycarbonate resin “trade name: Iupilon (registered trademark) H-4000” (viscosity average molecular weight 16,000, terminal hydroxyl group content 100 ppm), a mixture, S-3000 / H-4000 = 55 / 45 (weight ratio), viscosity average molecular weight 18,500

  Untreated PET1: Mitsubishi Chemical Corporation PET “GG500S”, using a germanium dioxide catalyst as a polycondensation catalyst, intrinsic viscosity [η]: 0.76 dl / g, terminal carboxyl group concentration AV: 28 μeq / g, ET ratio: 97.8 equivalent%, solid phase polymerization rate Ks: 0.0086 dl / g · hr (physical property values are all determined by the measurement method described later.)

  Untreated PET2: Mitsubishi Chemical Co., Ltd. PET "Novapex (registered trademark) RF543DE", using a titanium-based catalyst as a polycondensation catalyst, intrinsic viscosity [η]: 0.74 dl / g, terminal carboxyl group concentration AV : 8.4 μeq / g, ET ratio: 97.6 equivalent%, solid phase polymerization rate Ks: 0.0078 dl / g · hr (all physical property values are according to the measurement method described later)

Deactivated PET1: The above-mentioned untreated PET1 was subjected to the following polycondensation catalyst deactivation treatment, intrinsic viscosity [η]: 0.75 dl / g, terminal carboxyl group concentration AV: 30 μeq / g, ET ratio : 97.8 equivalent%, solid phase polymerization rate Ks: 0.0032 dl / g · hr (physical property values are all determined by the measurement method described later.)
<Deactivation method>
50 kg of untreated PET was boiled in 50 kg of distilled water at 100 ° C. for 1 hour, dehydrated, and dried in a nitrogen atmosphere at 120 ° C. for 6 hours.

Deactivated PET2: Untreated PET2 subjected to the deactivation treatment of the following polycondensation catalyst, intrinsic viscosity [η]: 0.73 dl / g, terminal carboxyl group concentration AV: 12 μeq / g, ET ratio : 97.6 equivalent%, solid phase polymerization rate Ks: 0.0042 dl / g · hr (all physical property values are according to the measurement method described later)
<Deactivation method>
0.01 parts by mass of the following phosphorus-based heat stabilizer 2 (ADK STAB AX-71) and 0.03 parts by mass of the following phosphorus-based heat stabilizer 1 (Irgaphos 168) are added to 100 parts by mass of untreated PET2. Then, after uniformly mixing with a tumbler mixer, using a twin screw extruder (manufactured by Nippon Steel Works, TEX30XCT, L / D = 42, number of barrels 12), cylinder temperature 270 ° C., screw rotation speed 200 rpm, discharge amount 15 kg The pellet of inactivated PET2 was produced by feeding to the extruder from the barrel at / hr and melt-kneading.

Deactivated PBT: Products produced by Mitsubishi Engineering Plastics Co., Ltd. PBT resin "Novaduran (registered trademark) 5020" is subjected to the following deactivation treatment of polycondensation catalyst
<Deactivation method>
0.1 parts by mass of the following phosphorus stabilizer 2 (Adeka Stub AX-71) and 0.03 parts by mass of the following phosphorus thermal stabilizer 1 (Irgaphos 168) are added to 100 parts by weight of the PBT resin, After mixing uniformly with a tumbler mixer, using a twin screw extruder (manufactured by Nippon Steel, TEX30XCT, L / D = 42, number of barrels 12), cylinder temperature 240 ° C., screw rotation speed 200 rpm, discharge rate 15 kg / hr The pellets of inactivated PBT were prepared by feeding from the barrel to the extruder and melting and kneading.

Phosphorus heat stabilizer 1: “Irgaphos 168” (Tris (2,4-di-t-butylphenyl) phosphite) manufactured by Ciba Specialty Chemicals Co., Ltd.
Phosphorus-based thermal stabilizer 2: “ADEKA STAB AX-71 (trade name)” manufactured by ADEKA (mono or di-stearyl acid phosphate)
Hindered phenol heat stabilizer: Ciba Specialty Chemicals “Irganox 1076” (octadecyl-3- (3,5-di-tert-butyl-4-hydroxyphenyl) propionate)

Elastomer A: “Product name: Staphyloid MG1011” (core / shell type elastomer made of butyl acrylate (core) / acrylonitrile-styrene copolymer (shell)) manufactured by Ganz Kasei Co., Ltd.
Elastomer B: Rohm and Haas “trade name: Paraloid EXL-2315” (core / shell type elastomer consisting of butyl acrylate (core) / polymethyl methacrylate (shell))
Elastomer C: “Product name: Methbrene S-2100” manufactured by Mitsubishi Rayon Co., Ltd. (core / shell type elastomer made of silicon acrylic (core) / polymethyl methacrylate (shell))
Elastomer D: “Product name: Tuftec H1041Z” (modified SEBS) manufactured by Asahi Kasei Corporation

Inorganic filler A: Glass fiber “trade name ECS03T-571” manufactured by Nippon Electric Glass Co., Ltd. (average fiber diameter 13 μm, average fiber length 3 mm)
Inorganic filler B: Glass fiber “trade name ECS03T-187” manufactured by Nippon Electric Glass Co., Ltd. (average fiber diameter 13 μm, average fiber length 3 mm, surface treated with glycidyl group on the surface (converged by bisphenol type epoxy resin)) )
Inorganic filler C: Glass fiber “trade name ECS03T-531DE” manufactured by Nippon Electric Glass Co., Ltd. (average fiber diameter 6 μm, average fiber length 3 mm, surface treated with glycidyl group on the surface (converged by bisphenol type epoxy resin)) )
Inorganic filler D: Glass fiber “trade name ECS03T-127” manufactured by Nippon Electric Glass Co., Ltd. (average fiber diameter 13 μm, average fiber length 3 mm, surface treated with glycidyl group on the surface (converged by bisphenol type epoxy resin)) (Contains more glycidyl groups than the inorganic filler B (T-187))
Inorganic filler E: Glass fiber “trade name ECS03T-511” manufactured by Nippon Electric Glass Co., Ltd. (average fiber diameter 13 μm, average fiber length 3 mm, surface treated with -COONa group (converged by bisphenol type epoxy resin)) fiber)
Inorganic filler F: Wollastonite “Nigloss 4W” manufactured by Niko Minerals (average fiber diameter 4.5 μm, average fiber length 50 μm, no surface treatment)

  Carbon black: “# 1000” furnace carbon black manufactured by Mitsubishi Chemical Corporation

  In addition, evaluation methods for various physical properties and characteristics are as follows.

<Terminal carboxyl group concentration of PET>
Weigh 0.5 g of resin chips accurately, dissolve in 25 ml of benzyl alcohol at 195 ° C., cool in ice water for several tens of seconds, add 2 ml of ethyl alcohol, and use an automatic titrator (“AUT-301” manufactured by Toa Denpa). And neutralized titration with 0.01N NaOH benzyl alcohol solution. From the measurement titration amount A (ml), the blank titration amount B (ml), the titer F of NaOH benzyl alcohol, and the weighed value W (g) of the sample, the amount of terminal carboxyl group AV (μeq / g) according to the following formula: Asked.
AV = (A−B) × 0.01 × F × 1000 / W

<Intrinsic viscosity of PET>
A solution having a concentration (c) of 1.0 g / dl was prepared using 0.50 g of freeze-pulverized PET sample using a mixed solution of phenol / tetrachloroethane (weight ratio 1/1) as a solvent. Here, the sample was dissolved at 120 ° C. for 30 minutes. The relative viscosity (η _rel ) of this solution with respect to the solvent alone (c = 0) was measured at 30 ° C. using an Ubbelohde viscometer, and this relative viscosity (η _rel ) -1 was _defined as the specific viscosity (η _sp ). The ratio (η _sp / c) to the concentration (c) was determined. Similarly, the concentration (c) is 0.5 g / dl, 0.2 g / dl, and 0.1 g / dl, and the respective ratios (η _sp / c) are obtained. From these values, the concentration (c) is set to 0. The ratio (η _sp / c) when extrapolated to was calculated as intrinsic viscosity [η] (dl / g).

<Composition analysis of PET>
¹ H-NMR was measured with a nuclear magnetic resonance apparatus (“JNM-EX270 type” manufactured by JEOL Ltd.) using a 3 wt% solution obtained by dissolving a resin sample in deuterated trifluoroacetic acid at room temperature, Assign the peak, determine the proportion of terephthalic acid and dicarboxylic acid components other than terephthalic acid, and ethylene glycol and other diol components from the integral ratio, and the content of oxyethyleneoxyterephthaloyl units (ET ratio) ) Was calculated.

<Solid-state polymerization rate of PET>
10 g of PET chip cut so that the average grain weight per grain becomes 24 mg is put in a container made of stainless steel mesh with a diameter of 30 mmφ and a height of 30 mm, and an inert oven (“IPHH-201 type” manufactured by ESPEC) It was dried at 160 ° C. for 4 hours under a nitrogen stream of 40 liters / minute. Thereafter, the temperature was raised from 160 ° C. to 210 ° C. over 1 hour while maintaining the nitrogen flow, and from the intrinsic viscosity [η] s after 3 hours after holding at 210 ° C., from the intrinsic viscosity [η] m after 2 hours. It was calculated by the following equation (1).
Solid phase polymerization rate Ks = ([η] s− [η] m) / 1 (1)

[Examples 1 to 21, Comparative Examples 1 to 7]
After each component shown in Tables 1 to 4 is uniformly mixed with a tumbler mixer in the ratios shown in Tables 1 to 4, a twin-screw extruder (manufactured by Nippon Steel Works, TEX30XCT, L / D = 42, barrel number 12) is used. The pellets of the resin composition were prepared by feeding to an extruder from a barrel at a cylinder temperature of 280 ° C., a screw rotation speed of 200 rpm, and a discharge rate of 30 kg / hr, and melt-kneading.

  After the pellets obtained by the above method were dried at 120 ° C. for 6 hours or more, using an injection molding machine (“M150AII-SJ type” manufactured by Meiki Seisakusho), the cylinder temperature was 280 ° C., the mold temperature was 80 ° C., Normal molding in which the resin does not stay in the cylinder under the molding cycle condition of 55 seconds, that is, the molten resin composition was injected into the cylinder, and the injection quantity was sufficient immediately after the filling amount was sufficient for injection molding ( In the case of no holding time), a test piece obtained under each condition was produced when molding was performed after holding in the cylinder for 60 minutes, and when molding was performed after holding in the cylinder for 30 minutes. (A test piece without holding time, a test piece after holding for 60 minutes, and a test piece after holding for 30 minutes). The shape of the test piece conformed to ISO 3167 multipurpose test piece type A.

<Number average molecular weight retention of resin composition>
The number average molecular weight Mn _x number-average molecular weight Mn _o and 60 minute hold after the test piece specimens without retention time obtained by the above-mentioned molding was measured, from these values, the holding of a number average molecular weight The rate (Mn _x / Mn _o × 100) was calculated.

The number average molecular weight was measured by the following method.
(Number average molecular weight of resin composition)
About 50 mg was cut out from the molded piece of the resin composition, immersed in chloroform so as to be 0.1 wt%, and allowed to stand at room temperature for 24 hours. This solution was filtered through a 0.45 μm polytetrafluoroethylene membrane filter to obtain a chloroform-soluble component for gel chromatography measurement. 0.1 ml of chloroform-soluble matter of the obtained resin composition was injected into Tosoh HLC-8220GPC (R), and GPC measurement was performed at a flow rate of 1.0 ml / min using chloroform as a mobile phase. PL 10 μm Mixed B (7.5 mm ID × 30 cm × 2) was used for the column, the column temperature was 40 ° C., and the built-in RI was used as a detector. A monodisperse polystyrene was used for the calibration sample, and the number average molecular weight was measured by a polystyrene conversion method. The measurement was performed twice per sample, and the average value of the two times was defined as the number average molecular weight Mn.

<Charpy impact strength of resin composition>
It was measured Charpy impact strength Ip _o notched compliant test piece without retention time obtained by the above-mentioned molding method ISO179 standard.

<Charpy impact strength retention ratio of resin composition>
The Charpy impact strength Ip _x of the test piece after 60 minutes retention obtained by the molding method described above was measured, retention of Charpy impact strength and a Charpy impact strength Ip _o specimens without retention times (Ip _x / Ip _o × 100) was calculated.

<MFR reduction rate of resin composition>
The test piece without holding time and the test piece held for 30 minutes formed by the above method were each cut with a pruning shear, and each was subjected to MFR (melt flow rate) measurement. The measurement conditions were 280 ° C. and a load of 2.16 kg, and conformed to ASTM D1238.
The MFR of the test piece after 30 minutes holding is set to [R _x ], the MFR of the test piece without holding time is set to [R _o ], and these values are used to calculate the MFR reduction rate based on the following formula. Calculated.
MFR decrease rate = ([R _o ] − [R _x ]) / [R _o ] × 100

<Elastic modulus of resin composition>
Based on ISO527, the elastic modulus of the resin composition was measured for the test piece without holding time.

<Appearance of molded product>
After holding for 60 minutes in the cylinder, the appearance of the molded product was visually observed for the ISO test piece obtained by the above-described molding method, and evaluated according to the following criteria.
(Double-circle): Silver, a foaming mark, etc. are not seen, but a glossy surface appearance is exhibited.
○: A glossy surface appearance is exhibited, but slight irregularities are observed near the gate.
X: Silver is generated on the most part of the surface, and the appearance without surface gloss is exhibited.

  The evaluation results are shown in Tables 1 to 4.

The following can be understood from Tables 1 to 4.
In Example 1, although the number average molecular weight retention rate is not high, the Charpy impact strength retention rate is high. In Examples 1 to 21 of the present invention, viscosity change due to stagnation during injection molding hardly occurs, heat stability and molding stability, excellent mechanical property balance such as Charpy impact strength and elastic modulus, and surface appearance are also excellent. You can see that
From Examples 1-5 and 11-17, it turns out that various things are applicable as polycarbonate resin.
From Example 6, it can be seen that various types of deactivated PET can be applied.
From Examples 3 and 4 and Examples 7 to 10, it can be seen that the blending ratio of polycarbonate resin and inactivated PET is effective within the scope of the present invention.
Examples 11 to 16 and 21 show that various inorganic fillers can be blended within the scope of the present invention.
From the results of Examples 11 to 15, the surface-treated inorganic filler is preferably used as the inorganic filler. In that case, the surface-treated inorganic filler containing a glycidyl group on the surface is more preferable than that containing a -COONa group on the surface. It turns out that it is preferable.
From the results of Examples 17 to 20, it can be seen that various elastomers can be blended within the scope of the present invention.

In Comparative Example 1, untreated PET was used, and the number average molecular weight retention rate, Charpy impact strength retention rate, and MFR reduction rate were inferior.
Comparative Example 2 does not contain an elastomer, and also results in poor number average molecular weight retention, Charpy impact strength retention, and MFR reduction.
Comparative Examples 3 and 4 do not contain a thermal stabilizer, resulting in poor number average molecular weight retention, Charpy impact strength retention, and MFR reduction.
In Comparative Example 5, deactivated PBT was used instead of deactivated PET, but the number average molecular weight retention rate, Charpy impact strength retention rate, and MFR reduction rate were inferior.
In Comparative Example 6, the blending amount of the elastomer exceeds the range of the present invention, and the Charpy impact strength retention rate is inferior, and the elastic modulus and the appearance of the molded product are remarkably inferior.
In Comparative Example 7, the amount of the inorganic filler compounded exceeds the range of the present invention, and the MFR reduction rate is inferior.

Claims (10)

  To 100 parts by mass of a resin component consisting of 95 to 30% by mass of a polycarbonate resin and 5 to 70% by mass of a polyethylene terephthalate resin, 0.01 to 0.5 parts by mass of a phosphorus-based heat stabilizer and / or a hindered phenol-based heat stabilizer. A polyethylene terephthalate resin in which 0.01 to 1 part by mass, 1 to 10 parts by mass of an elastomer and 1 to 20 parts by mass of an inorganic filler are blended, and the polyethylene terephthalate resin has been subjected to a deactivation treatment of a polycondensation catalyst. A polycarbonate / polyethylene terephthalate composite resin composition characterized in that: 2. The polyethylene terephthalate resin subjected to the deactivation treatment of the polycondensation catalyst according to claim 1, wherein the terminal carboxyl group concentration is 5 to 40 μeq / g, the intrinsic viscosity [η] is 0.6 to 1.5 dl / g, The ratio of the oxyethyleneoxyterephthaloyl unit to the repeating unit is 90 equivalent% or more, and the solid phase polymerization rate Ks calculated by the following formula (1) is 0.006 (dl / g · hr) or less. A polycarbonate / polyethylene terephthalate composite resin composition.
Solid-phase polymerization rate Ks = ([η] s− [η] m) / T (1)
(Where [η] s is the intrinsic viscosity (dl / g) of the polyethylene terephthalate resin after holding the polyethylene terephthalate resin at 210 ° C. for 3 hours under a nitrogen stream, and [η] m is a nitrogen stream. (Inherent viscosity (dl / g) of the polyethylene terephthalate resin after being kept at 210 ° C. for 2 hours, T is 1 (hour).)   3. The polycarbonate / polyethylene terephthalate composite resin composition according to claim 1, wherein the elastomer is a core / shell type elastomer.   4. The polycarbonate / polyethylene terephthalate composite resin composition according to claim 3, wherein the shell portion of the core / shell type elastomer is a polymethyl methacrylate-based polymerized or copolymerized block.   The polycarbonate / polyethylene terephthalate composite resin composition according to any one of claims 1 to 4, wherein the inorganic filler is a glass fiber.   6. The polycarbonate / polyethylene terephthalate composite resin composition according to claim 5, wherein the glass fiber has a glycidyl group on its surface. As a resin component, it contains polycarbonate resin 95-30 mass% and polyethylene terephthalate resin 5-70 mass%, 1-10 mass parts of elastomer and 1-20 mass parts of inorganic fillers with respect to 100 mass parts of the resin component. a polycarbonate / polyethylene terephthalate composite resin composition comprising a number average molecular weight Mn _x chloroform solubles was held 60 minutes at 280 ° C. has a number average of chloroform-soluble component before holding for 60 minutes at 280 ° C. polycarbonate / polyethylene terephthalate composite resin composition which is characterized in that at least 80% of the molecular weight Mn _o. As a resin component, it contains polycarbonate resin 95-30 mass% and polyethylene terephthalate resin 5-70 mass%, 1-10 mass parts of elastomer with respect to 100 mass parts of resin components, and 1-20 mass parts of inorganic fillers. it a polycarbonate / polyethylene terephthalate composite resin composition, 280 ° C. Charpy impact strength Ip _x after holding for 60 minutes is 80% or more of the preceding Charpy impact strength Ip _o holding 60 minutes at 280 ° C. containing A polycarbonate / polyethylene terephthalate composite resin composition. As a resin component, it contains polycarbonate resin 95-30 mass% and polyethylene terephthalate resin 5-70 mass%, 1-10 mass parts of elastomer with respect to 100 mass parts of resin components, and 1-20 mass parts of inorganic fillers. A polycarbonate / polyethylene terephthalate composite resin composition containing [R _x ] of the molded product injection-molded after holding the resin composition at 280 ° C. for 30 minutes and injecting the resin composition into the injection molding machine upon immediately MFR of injection molded molded article after the _{[R o],} that decreasing rate of MFR _{[R x]} for MFR _{[R o]} is calculated by the following formula (3) is -20 to 20% A polycarbonate / polyethylene terephthalate composite resin composition.
Reduction rate of MFR [%] = (R _o −R _x ) / R _o × 100 (3)   A polycarbonate / polyethylene terephthalate composite resin molded article obtained by molding the polycarbonate / polyethylene terephthalate composite resin composition according to any one of claims 1 to 9.