JP2017071729A - Thermoplastic polyester resin composition, and light reflector using the same - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a thermoplastic polyester resin composition which not only can provide a molded article that is suitable for forming a light reflection surface of a light reflector, is excellent in surface smoothness and has low fogging performance but also is excellent in heat resistance and can suppress mold staining when continuously molded.SOLUTION: There are provided a thermoplastic polyester resin composition which is a resin composition that contains 100-50 pts.mass of a polybutylene terephthalate resin (A) and 0-50 pts.mass of a polyethylene terephthalate resin (B), and contains calcium carbonate (C) that has an average particle size of 0.05-2 μm and is surface-treated, kaolin (D) having an average particle size of 0.05-2 μm, and a polyfunctional glycidyl group-containing styrenic polymer (E), where the sum of the content of (C) and (D) is 1-20 pts.mass with respect to 100 pts.mass of the total polyester resin contained in the resin composition, and a content of (E) is 0.05-3 pts.mass; and a component for light reflector and a light reflector manufactured by using the same.SELECTED DRAWING: None

Description

  The present invention is, for example, a thermoplastic polyester resin composition used for a light reflector part in which a light reflecting layer is provided on a surface in a part constituting an automotive lamp or a lighting fixture, and a light reflector part comprising the same. The present invention also relates to a light reflector in which a light reflecting metal layer is directly formed on a part or the whole of the light reflector component.

  Light reflectors such as extensions and reflectors used in automobile lamps and lighting fixtures are required to have high luminance appearance, uniform reflectivity, and heat resistance against heat generated by light from a light source. Conventionally, such products have been provided with a metal thin film on the surface of a bulk molding compound (hereinafter abbreviated as BMC) which is a thermosetting resin.

  Although BMC is excellent in heat resistance, dimensional stability, etc., the molding cycle is long, and it takes time to process burrs during molding. There was a problem. As means for improving these problems, studies using thermoplastic resins have been conducted.

  As an example of using a thermoplastic resin, a composition in which various reinforcing materials are blended with a crystalline resin typified by a polyester resin such as polybutylene terephthalate or polyethylene terephthalate, or an amorphous resin typified by a polycarbonate resin. Has been proposed. In particular, for light reflectors that require mechanical properties, electrical properties, heat resistance, good moldability, etc., various reinforcing materials are applied to polybutylene terephthalate resin alone or a mixture of polybutylene terephthalate and other resins. The blended composition is widely adopted.

  As a technique for forming a metal thin film or the like to give a performance as a light reflector to a molded article made of the thermoplastic resin composition described above, pretreatment by undercoat treatment before forming a light reflective metal layer on the molded article The method of performing is mentioned. In the conventional method for performing the undercoat treatment, since an organic solvent is used in the undercoat, the burden on the environment is large. Further, the organic solvent volatilizes and the coat needs time to be cured. The cost for the process is high, and the total cost is a problem. Therefore, there is a need for a thermoplastic resin composition for a light reflector that does not require a pretreatment step and that can be directly formed by directly forming a metal layer.

  When performing direct vapor deposition by the direct method, it is necessary that the resin molded product itself has good surface smoothness, high glossiness, and brightness. Therefore, a material in which gas generated during molding is suppressed is necessary. If the continuous molding is continued as the number of moldings increases, mold contamination will occur due to resin degradation products and mold release agent degradation products that occur during molding. It may be transferred and the appearance of the molded product may be impaired. In particular, high brightness appearance, uniform reflectivity, and the like are required for components that make up automotive lamps and lighting fixtures, and components for light reflectors that have a light reflecting layer on the surface. Therefore, in these applications, it is necessary to frequently clean the mold, and a molding material in which mold contamination is suppressed is demanded.

  Further, with regard to automobile lamps, in order to achieve low fuel consumption of automobiles, weight reduction of large-sized automobile lamps is a major issue. The light reflector, which is a component, is also required to be lightweight, and a low specific gravity of resin is an important required characteristic.

  As resin compositions that can be vapor-deposited by the direct method, for example, there are those proposed in Patent Documents 1 and 2, but in Patent Documents 1 and 2, in order to improve the heat resistance after vapor deposition, Although selection has been made, gas generation during molding is accompanied by a large amount of gas generation from the resin, and mold contamination cannot be suppressed. Further, Patent Document 3 examines gas generation during continuous molding including heat resistance of the mold release agent, but only studies on selection of the mold release agent have been made.

  Furthermore, in order to improve the dimensional stability of the product, various inorganic filler blends have been proposed. For example, Patent Document 4 proposes that about 10% by mass of fine spherical inorganic fillers such as barium sulfate and titanium oxide are blended, but the aggregation of fillers may occur and the appearance may be impaired. In addition, in barium sulfate, titanium oxide, and the like, the weight of the molded product may be too heavy because the specific gravity of the filler is large.

JP 2008-280498 A JP 2009-102581 A JP 2010-189484 A JP 2009-235156 A

  The object of the present invention is not only to provide a molded article that is suitable for the formation of a light reflecting surface of a light reflector, is excellent in surface smoothness, has low fogging properties, and is lightweight, but also has a mold when continuously molded. An object of the present invention is to provide a thermoplastic polyester resin composition that can suppress dirt and is excellent in heat resistance.

  As a result of intensive studies, the present inventors have found that the object can be achieved if a specific polyester resin is used as a matrix and a specific calcium carbonate and kaolin, a polyfunctional glycidyl group-containing styrene polymer or the like is blended, and the present invention has been completed. .

That is, the present invention is as follows.
[1]
A resin composition containing 100 to 50 parts by mass of a polybutylene terephthalate resin (A) and 0 to 50 parts by mass of a polyethylene terephthalate resin (B), and is subjected to a surface treatment having an average particle diameter of 0.05 to 2 μm. 100% polyester resin containing calcium carbonate (C), kaolin (D) having an average particle diameter of 0.05 to 2 μm, and polyfunctional glycidyl group-containing styrenic polymer (E). A thermoplastic polyester resin composition in which the sum of the contents of (C) and (D) is 1 to 20 parts by mass and the content of (E) is 0.05 to 3 parts by mass per part by mass.
[2]
The thermoplastic polyester resin according to [1], wherein the surface treatment of the component (C) is one or more selected from silica treatment, epoxy silane coupling agent treatment, and alkyl silane coupling agent treatment. Composition.
[3]
[1] The surface treatment of the component (C) is any one of silica treatment, composite treatment of silica treatment and epoxysilane coupling agent treatment, and composite treatment of silica treatment and alkylsilane coupling agent treatment. A thermoplastic polyester resin composition.
[4]
The thermoplastic polyester resin composition according to any one of [1] to [3], containing 0.01 to 5 parts by mass of a phosphorus compound (F) per 100 parts by mass of the total polyester resin.
[5]
A component for a light reflector comprising the thermoplastic polyester resin composition according to any one of [1] to [4].
[6]
A light reflector in which a light-reflecting metal layer is directly formed on at least a part of the surface of the light reflector component according to [5].
[7]
[Manufacturing a component for a light reflector including a step of injecting and molding the thermoplastic polyester resin composition according to any one of [1] to [4] into a mold in which at least a part of the inner surface is a mirror surface. Method.
[8]
At least polybutylene terephthalate resin (A), polyethylene terephthalate resin (B), surface-treated calcium carbonate (C) having an average particle size of 0.05 to 2 μm, and kaolin having an average particle size of 0.05 to 2 μm (D) is a method for producing a thermoplastic polyester resin composition having a step of melt-kneading the polyfunctional glycidyl group-containing styrene polymer (E), and the blending ratio of (B) is (A) 100 to 50 mass. (B) is 0 to 50 parts by mass with respect to parts, and the mixing ratio of (C), (D), and (E) is (C) and (D) per 100 parts by mass of the total polyester resin contained in the resin composition. ) Is 1 to 20 parts by mass and (E) 0.05 to 3 parts by mass, the method for producing a thermoplastic polyester resin composition according to any one of [1] to [4].
[9]
The method for producing a thermoplastic polyester resin composition according to [8], wherein a polybutylene terephthalate resin having a titanium atom content of 60 ppm or less is used as the polybutylene terephthalate resin (A).
[10]
The method for producing a thermoplastic polyester resin composition according to [8] or [9], wherein a polyethylene terephthalate resin having an acid value of 30 eq / ton or less is used as the polyethylene terephthalate resin (B).

  The thermoplastic polyester resin composition of the present invention is not only excellent in light weight and surface specularity, but also highly resistant to mold fouling during continuous molding. Excellent in properties. Further, the obtained molded product is excellent in low fogging property.

Hereinafter, the present invention will be described in detail.
The polybutylene terephthalate resin (A) in the present invention is a general polymerization method such as a polycondensation reaction mainly comprising terephthalic acid or an ester-forming derivative thereof and 1,4-butanediol or an ester-forming derivative thereof. It is a polymer obtained by. The polymer is preferably a polymer having a butylene terephthalate repeating unit of 80 mol% or more, more preferably 90 mol% or more, still more preferably 95 mol% or more, and most preferably 100 mol%. Other copolymer components may be included in a range that does not impair the characteristics, for example, about 20% by mass or less. Examples of the copolymer that can be used as the polybutylene terephthalate resin (A) include polybutylene (terephthalate / isophthalate), polybutylene (terephthalate / adipate), polybutylene (terephthalate / sebacate), polybutylene (terephthalate / decane dicarboxylate). ), Polybutylene (terephthalate / naphthalate), poly (butylene / ethylene) terephthalate, and the like. The polybutylene terephthalate resin (A) may be a single resin or a mixture of two or more resins.

  The polybutylene terephthalate resin (A) of the present invention is obtained by using a titanium catalyst in the esterification reaction (or transesterification reaction) between 1,4-butanediol and terephthalic acid (or dialkyl terephthalate). The titanium atom content is preferably 60 mg / kg or less.

  As the titanium catalyst, a titanium compound is usually used. Specific examples thereof include inorganic titanium compounds such as titanium oxide and titanium tetrachloride, titanium alcoholates such as tetramethyl titanate, tetraisopropyl titanate, and tetrabutyl titanate, and tetraphenyl titanate. And titanium phenolate. Among these, tetraalkyl titanates are preferable, and tetrabutyl titanate is particularly preferable among them.

  In the polybutylene terephthalate resin (A) of the present invention, the lower limit of the titanium content is preferably 5 mg / kg, more preferably 8 mg / kg, and even more preferably 15 mg / kg. A preferable upper limit of the titanium content is 45 mg / kg, more preferably 40 mg / kg, and particularly preferably 35 mg / kg. When the content of titanium is greater than 60 mg / kg, the effect of suppressing mold stains during continuous molding tends to be difficult to develop.

  Titanium and tin may be used together as a catalyst. In addition to or in place of titanium and tin, magnesium compounds such as magnesium acetate, magnesium hydroxide, magnesium carbonate, magnesium oxide, magnesium alkoxide, magnesium hydrogen phosphate, calcium hydroxide, calcium carbonate Reaction of calcium compounds such as calcium oxide, calcium alkoxide and calcium hydrogen phosphate, antimony compounds such as antimony trioxide, germanium compounds such as germanium dioxide and germanium tetroxide, manganese compounds, zinc compounds, zirconium compounds and cobalt compounds A catalyst, a phosphoric acid, phosphorous acid, hypophosphorous acid, polyphosphoric acid, phosphorus compounds such as esters and metal salts thereof, and a reaction aid such as sodium hydroxide may be used.

  The content of titanium atoms or the like can be measured using a method such as atomic emission, atomic absorption, Inductively Coupled Plasma (ICP) after recovering the metal in the polymer by a method such as wet ashing.

  The intrinsic viscosity of the polybutylene terephthalate resin (A) in the present invention is preferably 0.5 to 1.6 dl / g, more preferably 0.6 to 1.2 dl / g, still more preferably 0.7 to 1. 0.0 dl / g. When the intrinsic viscosity is less than 0.5 dl / g, the extrudability deteriorates, leading to resin drawdown and uneven molding, and when it exceeds 1.6 dl / g, the melt viscosity becomes high, Fluidity deteriorates. In addition, said intrinsic viscosity is the value measured at 30 degreeC using the mixed solvent of phenol / tetrachloroethane (mass ratio 1/1).

  The terminal carboxyl group of the polybutylene terephthalate resin plays a catalytic role in the hydrolysis reaction of the polymer, and the hydrolysis is accelerated as the amount of the terminal carboxyl group increases. Therefore, the terminal carboxyl group concentration is preferably low. The terminal carboxyl group concentration of the polybutylene terephthalate resin (A) in the present invention is preferably 40 eq / ton or less, more preferably 30 eq / ton or less, still more preferably 25 eq / ton or less, and particularly preferably 20 eq / ton or less.

  On the other hand, since the terminal hydroxyl group of the polybutylene terephthalate resin causes back-biting and serves as a starting point for producing tetrahydrofuran and a cyclic oligomer, the terminal hydroxyl group concentration is preferably low in order to suppress back-biting. The terminal hydroxyl group concentration of the polybutylene terephthalate resin (A) in the present invention is preferably 110 eq / ton or less, more preferably 90 eq / ton or less, still more preferably 70 eq / ton or less, and particularly preferably 50 eq / ton or less. is there.

  The method for adjusting the terminal carboxyl group concentration and the terminal hydroxyl group concentration of the polybutylene terephthalate resin (A) is not particularly limited. For example, a method for adjusting the charging ratio of the acid component / glycol component when polymerizing the polybutylene terephthalate resin, A method of adding an end-capping agent during polymerization of butylene terephthalate resin, a method of heat treatment under vacuum or nitrogen atmosphere after polymerization of polybutylene terephthalate resin, a solid-phase polymerization operation for polybutylene terephthalate resin, etc. A method can be mentioned. Moreover, you may combine the illustrated method and other methods.

  In the method of adding a terminal blocking agent during the polymerization, if a terminal blocking agent that reacts with a carboxyl group is used, the carboxyl group terminal concentration can be lowered, and if a terminal blocking agent that reacts with a hydroxyl group is used, the hydroxyl group concentration Can be reduced. Also, in the method of heat treatment after polymerization, the terminal hydroxyl group concentration is low and the terminal carboxyl group concentration tends to be high by intentionally causing back-biting of the terminal butanediol component. The heat treatment may be carried out in a molten state immediately after the polymerization after the polymerization, or may be carried out in a pellet state after the removal. In view of production efficiency, it is preferable to carry out the polymer in a molten state immediately after the polymerization, just after the polymerization, because the back-biting reaction rate is high. In this method, the terminal carboxyl group concentration and terminal hydroxyl group concentration can be adjusted by the heat treatment temperature and time. In the case of solid-phase polymerization, esterification or transesterification reaction proceeds, and both terminal carboxyl group concentration and terminal hydroxyl group concentration tend to decrease, but the molecular weight also increases accordingly, so adjustment of solid-state polymerization temperature and time is necessary. It is.

  The polyethylene terephthalate resin (B) used in the present invention is a polymer obtained by an ordinary polymerization method such as a polycondensation reaction containing terephthalic acid or its ester-forming derivative and ethylene glycol or its ester-forming derivative as main components. It is a coalescence. The polymer is preferably a polymer having an ethylene terephthalate repeating unit of 80 mol% or more, more preferably 90 mol% or more, still more preferably 95 mol% or more, and most preferably 100 mol%. Other copolymer components may be included in a range that does not impair the characteristics, for example, about 20% by mass or less. Examples of copolymers that can be used as the polyethylene terephthalate resin (B) include polyethylene (terephthalate / isophthalate), polyethylene (terephthalate / adipate), polyethylene (terephthalate / sebacate), polyethylene (terephthalate / decanedicarboxylate). , Polyethylene (terephthalate / naphthalate), poly (ethylene / cyclohexanedimethyl) / terephthalate, poly (butylene / ethylene) terephthalate, and the like may be used alone or in combination of two or more. By using the polyethylene terephthalate resin (B), the moldability and the direct metal vapor deposition property can be made higher compatible.

  The polyethylene terephthalate resin (B) used in the present invention has an intrinsic viscosity of 0.3 to 1.6 dl / g when measured at 30 ° C. using a mixed solvent of phenol / tetrachloroethane (mass ratio 1/1). Preferably in the range of 0.45 to 1.35 dl / g, more preferably in the range of 0.5 to 1.2 dl / g, 0.55 Those in the range of ˜1.05 dl / g are most preferred. When the intrinsic viscosity of the polyethylene terephthalate resin (B) is 0.3 to 1.6 dl / g, the mechanical properties and moldability of the thermoplastic polyester resin composition of the present invention are improved.

  The terminal carboxyl group of the polyethylene terephthalate resin plays a catalytic role in the hydrolysis reaction of the polymer, and the hydrolysis is accelerated as the amount of the terminal carboxyl group increases, so that the terminal carboxyl group concentration is preferably low. The terminal carboxyl group concentration of the polyethylene terephthalate resin (B) used in the present invention is 30 eq / ton or less, preferably 25 eq / ton or less, more preferably 20 eq / ton or less, and still more preferably 10 eq / ton or less.

  The method for adjusting the terminal carboxyl group concentration of the polyethylene terephthalate resin (B) is not particularly limited. For example, the method for adjusting the charging ratio of the acid component / glycol component when polymerizing the polyethylene terephthalate resin, during the polymerization of the polyethylene terephthalate resin Examples thereof include a method of adding a terminal blocking agent and a method of further performing a solid phase polymerization operation on the polyethylene terephthalate resin. Moreover, you may combine the illustrated method and other methods. In the method of adding a terminal blocking agent during the polymerization, if a terminal blocking agent that reacts with a carboxyl group is used, the carboxyl group terminal concentration can be lowered. In the case of solid-phase polymerization, esterification or transesterification proceeds, and the terminal carboxyl group concentration decreases. However, the molecular weight also increases with this, so it is necessary to adjust the solid-phase polymerization temperature and time.

  The blending amount of the polybutylene terephthalate resin (A) and the polyethylene terephthalate resin (B) in the present invention is 0 to 50 parts by mass of the component (B) with respect to 100 to 50 parts by mass of the component (A), preferably ( (A) 100 to 60 parts by weight of component (B) 0 to 40 parts by weight of component, more preferably (A) 90 to 70 parts by weight of component (B) 10 to 30 parts by weight, more preferably ( It is 15-25 mass parts of (B) component with respect to 85-75 mass parts of A) component. It is possible to improve the surface appearance of the molded product obtained from the resin composition of the present invention by blending the component (B), but when the blending amount exceeds 50 parts by mass, the mold release at the time of injection molding of the resin composition The properties are poor and the molding high cycle property is poor, and the heat resistance of the resin tends to decrease.

  Moreover, the polyester contained in the thermoplastic polyester resin composition of the present invention may contain a thermoplastic polyester resin (G) other than (A) and (B). The polyester resin (G) is a polyester resin having a chemical structure that can be obtained by polycondensation of an aromatic or alicyclic dicarboxylic acid or an ester-forming derivative thereof with a diol. Examples of the dicarboxylic acid component constituting the polyester resin (G) include terephthalic acid, isophthalic acid, naphthalenedicarboxylic acid, and cyclohexanedicarboxylic acid. Examples of the diol component constituting the polyester resin (G) include alkylene diols such as ethylene glycol, diethylene glycol, propane diol, butane diol, and neopentyl glycol, and ethylene oxide diadducts of bisphenol A.

  Specific examples of the polyester resin (G) include polypropylene terephthalate, polyethylene naphthalate, polybutylene naphthalate, and polypropylene naphthalate.

  The total amount of polybutylene terephthalate resin (A) and polyethylene terephthalate resin (B) with respect to all the polyester resins contained in the thermoplastic polyester resin composition of the present invention is 80 with respect to the good surface smoothness of the molded product. It is preferably at least 90% by mass, more preferably at least 90% by mass, even more preferably at least 95% by mass, and may be 100% by mass.

  Calcium carbonate (C) in the present invention, among various inorganic fillers, from the aspects of specific gravity, particle diameter, dispersibility in resin composition, handling properties, availability, etc., and parts for light reflectors, and It is most suitable for a light reflector in which a light reflecting metal layer is directly formed on a part or the whole of the light reflector component.

  The calcium carbonate (C) in the present invention is light or heavy calcium carbonate. Light calcium carbonate is synthetic calcium carbonate, and heavy calcium carbonate is natural calcium carbonate. Calcium carbonate (C) in the present invention has an average particle size measured by electron microscopy of 0.05 to 2 μm, more preferably 0.1 to 1 μm, still more preferably 0.1 to 0.3 μm, particularly Preferably it is 0.1-0.2 micrometer or less. When the average particle diameter exceeds 2 μm, the surface smoothness of the obtained molded product tends to be inferior, and when it is less than 0.05 μm, aggregation tends to occur in the composition. In addition, since heavy calcium carbonate is pulverized from natural minerals, it is difficult to produce those having an average particle size of less than 1 μm, and light calcium carbonate that can easily produce those having an average particle size of less than 1 μm is more preferable.

The calcium carbonate (C) in the present invention needs to be surface-treated in order to enhance dispersibility in the resin composition. As the surface treatment, treatment with a surface treatment agent such as aminosilane coupling agent, epoxysilane coupling agent, titanate coupling agent, aluminate coupling agent, treatment with silica, treatment with fatty acid, SiO ₂ -Al ₂ O _{3 and} neutralization treatment with an acidic compound such as a phosphorus compound. These treatments may be combined. From the viewpoint of fogging properties, treatment with silica, treatment with an epoxy silane coupling agent, treatment with an alkyl silane coupling agent, treatment with silica, treatment with an alkyl silane coupling agent, and treatment with silica are more preferred. Is most preferred. Further, combined treatment of silica treatment and epoxy silane coupling agent treatment, and combined treatment of silica treatment and alkylsilane coupling agent treatment are most preferable.

  Furthermore, the surface treatment method of calcium carbonate (C) is not particularly limited, and examples thereof include a method of physically mixing calcium carbonate (C) and each treatment agent. For example, a roll mill, high-speed rotary grinding Or a pulverizer such as a jet mill, or a mixer such as a Nauta mixer, a ribbon mixer, or a Henschel mixer can be used.

  The kaolin (D) in the present invention means hydrous kaolin and calcined kaolin. The hydrous kaolin is kaolin containing hydrated water in the crystal, and the calcined kaolin is calcined hydrous kaolin at a high temperature to release hydrated water. It is about kaolin. The kaolin (D) in the present invention is a component for light reflectors and various parts of various inorganic fillers in terms of specific gravity, particle diameter, dispersibility in a resin composition, handling properties, availability, and the like. It is most suitable for a light reflector in which a light reflecting metal layer is directly formed on a part or the whole of a light reflector component.

  The kaolin (D) in the present invention has an average particle size of 0.05 to 2 μm, more preferably 0.1 to 1 μm, still more preferably 0.1 to 0.8 μm, as measured by an X-ray transmission precipitation method. Particularly preferably, the thickness is 0.1 to 0.5 μm. When the average particle diameter exceeds 2 μm, the surface smoothness of the obtained molded product tends to be inferior. If it is less than 0.05 μm, aggregation tends to occur in the composition.

  The kaolin (D) in the present invention is used for improving the heat resistance and rigidity required as a light reflector of the resin composition. Kaolin is excellent in heat resistance, rigidity, and dimensional stability because of its scale-like shape.

  The kaolin (D) in the present invention can be subjected to any surface treatment in order to improve dispersibility. Examples of the surface treatment include treatment with a surface treatment agent such as an aminosilane coupling agent, an epoxysilane coupling agent, a titanate coupling agent, and an aluminate coupling agent, treatment with a fatty acid, and the like. Also good.

  Furthermore, the surface treatment method of kaolin (D) is not particularly limited, and examples thereof include a method of physically mixing kaolin (D) and each treatment agent, such as a roll mill, a high-speed rotary grinder, A pulverizer such as a jet mill or a mixer such as a Nauta mixer, a ribbon mixer, and a Henschel mixer can be used.

  Calcium carbonate (C) and kaolin (D) in the present invention are used for improving heat resistance and rigidity required as a light reflector of the resin composition. Calcium carbonate (C) has good dispersibility due to its surface treatment and is particularly excellent in surface smoothness, and kaolin is excellent in heat resistance, rigidity and dimensional stability because of its scale-like shape. By using these together, it is possible to impart characteristics suitable for the light reflector part and the light reflector in which the light reflecting metal layer is directly formed on a part or the whole of the light reflector part.

The content of calcium carbonate (C) and kaolin (D) is the sum of calcium carbonate (C) and kaolin (D) with respect to 100 parts by mass of the total polyester resin contained in the thermoplastic polyester resin composition of the present invention. 1 part by mass or more, preferably 2 parts by mass or more, and more preferably 4 parts by mass or more. However, in order to increase the surface smoothness of the obtained molded product, the total content of calcium carbonate (C) and kaolin (D) needs to be 20 parts by mass or less, particularly 15 parts by mass or less. Preferably, 10 parts by mass or less is more preferable. If it exceeds 20 parts by mass, the surface smoothness of the resulting molded product may be lowered due to the embossing of the filler, and may be whitened after vapor deposition.
The ratio of calcium carbonate (C) and kaolin (D) is not particularly limited, but the mass ratio is preferably 0/100 <(D) / (C) ≦ 100/100, and 20/100 ≦ (D) / (C) ≦ 80/100 is more preferable, and 30/100 ≦ (D) / (C) ≦ 70/100 is more preferable.
In the range which does not impair the effect of this invention, you may contain inorganic fillers other than (C) and (D) in a thermoplastic polyester resin composition. In that case, the average particle diameter of the inorganic filler other than (C) and (D) is preferably 3 μm or less, and more preferably 2 μm or less. When the total amount of the inorganic filler is 100% by mass, the total of (C) and (D) is preferably in the range of 80% by mass or more.

The polyfunctional glycidyl group-containing styrene polymer (E) used in the present invention is a polyfunctional glycidyl styrene acrylic polymer having a weight average molecular weight (Mw) of 1000 or more and an epoxy value of 0.5 meq / g or more. Is preferred. At this time, the weight average molecular weight (Mw) is more preferably 5000 or more, further preferably 7000 or more, and particularly preferably 8000 or more. If the weight average molecular weight (Mw) is less than 1000, the number of glycidyl groups per molecule decreases, and the trapping effect of the free organic carboxylic acid and the like contained in the polyester resin oligomer, monomer, and fatty acid ester release agent decreases. Therefore, it is not preferable. The weight average molecular weight (Mw) is preferably 50000 or less from the viewpoint of compatibility with the polyester resin. The epoxy value is more preferably 0.6 meq / g or more, and further preferably 0.65 meq / g or more. If the epoxy value is less than 0.5 meq / g, the trapping effect of the polyester resin oligomer, monomer, free organic carboxylic acid, etc. is lowered, which is not preferable. The epoxy value is preferably 3 meq / g or less from the viewpoint of suppressing excessive reaction with the polyester resin. The polyfunctional glycidyl group-containing styrene-based polymer (E) used in the present invention contains 0.05 to 3 parts by mass with respect to 100 parts by mass of the total polyester contained in the thermoplastic polyester resin composition of the present invention.
By making the polyfunctional glycidyl group-containing styrenic polymer (E) within this range, it is possible to efficiently capture gasification components such as polyester oligomers, monomers, and free organic carboxylic acids, and excellent low gas properties Can be realized.

The polyfunctional glycidyl group-containing styrenic polymer (E) used in the present invention is preferably one having good compatibility with the polyester resin and a small refractive index difference from the polyester resin. The weight average molecular weight (Mw) is 1000 or more, and the epoxy value is preferably 0.5 meq / g or more, more preferably 1.0 meq / g or more.
As a specific component of the polyfunctional glycidyl group-containing styrene polymer (E), a copolymer of a glycidyl group-containing unsaturated monomer and a vinyl aromatic monomer is preferable.

  Examples of the glycidyl group-containing unsaturated monomer include unsaturated carboxylic acid glycidyl ester, unsaturated glycidyl ether, and the like, and examples of unsaturated carboxylic acid glycidyl ester include glycidyl acrylate, glycidyl methacrylate, monoglycidyl itaconate. Examples of the ester include glycidyl methacrylate. Examples of the unsaturated glycidyl ether include vinyl glycidyl ether, allyl glycidyl ether, 2-methylallyl glycidyl ether, and methacryl glycidyl ether, with methacryl glycidyl ether being preferred.

  Examples of the vinyl aromatic monomer include styrene monomers such as styrene, methylstyrene, dimethylstyrene, and ethylstyrene, and styrene is preferable.

The copolymerization ratio of the glycidyl group-containing unsaturated monomer and the vinyl aromatic monomer is such that the copolymerization amount of the glycidyl group-containing unsaturated monomer is preferably 1 to 30% by mass, and more preferably. Is 2 to 20% by mass.
When the copolymerization amount of the glycidyl group-containing unsaturated monomer is less than 1% by mass, the trapping effect of the polyester resin oligomer, monomer, free organic carboxylic acid and the like tends to be small, and the low gas property tends to be adversely affected. When it exceeds 30 mass%, the stability as a resin composition may be impaired.

  C1-C7 alkyl ester of acrylic acid or methacrylic acid, for example (meth) acrylic such as methyl, ethyl, propyl, isopropyl, butyl ester of (meth) acrylic acid, as long as compatibility with polyester resin is not impaired Acid ester monomers, (meth) acrylonitrile monomers, vinyl ester monomers such as vinyl acetate and vinyl propylate, (meth) acrylamide monomers, maleic anhydride, maleic acid monoesters, diesters, etc. A monomer or the like may be copolymerized. However, α-olefins such as ethylene, propylene, and butene-1 are preferably not copolymerized because compatibility with the polyester resin tends to be impaired.

  If the polyfunctional glycidyl group-containing styrenic polymer (E) is more than 3 parts by mass, gelation may be caused by reaction with the polyester resin. Further, when the polyfunctional glycidyl group-containing styrenic polymer (E) is less than 0.05 parts by mass, the trapping effect of the polyester resin oligomer, monomer, free organic carboxylic acid, etc. is reduced, and the low gas property is impaired. There is a case. The blending amount of the polyfunctional glycidyl group-containing styrenic polymer (E) is preferably 0.1 to 2 parts by mass with respect to 100 parts by mass of the total polyester resin contained in the thermoplastic polyester resin composition of the present invention. 0.15 to 1 part by mass is more preferable.

  The phosphorus compound (F) in the present invention is used as an antioxidant, a peroxide scavenger, and an inert agent for a titanium catalyst. Phosphoric acid, phosphorous acid, phosphinic acid, phosphonic acid, and those And derivatives thereof. Specifically, inorganic phosphates such as monosodium phosphate, disodium phosphate, trisodium phosphate, sodium phosphite, calcium phosphite, magnesium phosphite, manganese phosphite, trimethyl phosphate, phosphorus Phosphoric acid esters such as acid tributyl ester, phosphoric acid triphenyl ester, phosphoric acid monomethyl ester or phosphoric acid dimethyl ester, triphenyl phosphite, trioctadecyl phosphite, tridecyl phosphite, trinonylphenyl phosphite, diphenylisodecyl phosphine Phyto, bis (2,6-di-tert-butyl-4-methylphenyl) pentaerythritol diphosphite (molecular weight 633. For example, trade name: ADK STAB PEP-36, available from ADEKA, the same applies hereinafter), bi (2,4-di-tert-butylphenyl) pentaerythritol diphosphite (“ADK STAB PEP-24G”, molecular weight 604), tris (2,4-di-tert-butylphenyl) phosphite, distearyl pentaerythritol diphosphite Phosphite (“Adekastab PEP-8”, molecular weight 733), bis (nonylphenyl) pentaerythritol diphosphite (“Adekastab PEP-4C”, molecular weight 633), tetra (tridecyl-4,4′-isopropylidenediphenyldiphos Phosphites, phosphorous acids such as 2,2-methylenebis (4,6-di-tert-butylphenyl) octyl phosphite, phosphinic acids such as dimethylphosphinic acid and phenylphosphinic acid, phenylphosphonic acid, phenylphosphonic acid dimethyl ester And phosphonic acids such as phenylphosphonic acid diethyl ester, etc. These can be used alone or in a mixture thereof Examples of metal deactivators include bisbenzylidene hydrazide oxalate (trade name: Inhibitor OABH). , Manufactured by Eastman), decamethylene dicarboxylic acid disalicyloyl hydrazide (trade name: ADK STAB CDA-6, manufactured by ADEKA), N, N′-bis [3- (3,5-di-t-butyl-4 -Hydroxyphenyl) propionyl] hydrazine (trade name: Irganox MD 1,024, manufactured by Ciba Geigy), 2,2′-oxamidobis [ethyl 3- (3,5-t-butyl-4-hydroxyphenyl) propionate] (product) Name: City of Naugard XL-1, manufactured by Shiraishi Calcium Co., Ltd.) Commercial products can be used.

  In the present invention, in order to further improve the releasability, it is preferable to contain a release agent. The release agent is not particularly limited as long as it can be used for polyester. For example, long chain fatty acids or esters thereof, metal salts, amide compounds, polyethylene wax, polyethylene oxide and the like can be mentioned. As the long chain fatty acid, those having 12 or more carbon atoms are particularly preferable, and examples thereof include stearic acid, 12-hydroxystearic acid, behenic acid, and montanic acid. Partial or total carboxylic acid may be monoglycol or polyglycol. It may be esterified or may form a metal salt. Examples of the amide compound include ethylene bisterephthalamide and methylene bisstearyl amide. Specific examples of these include Rikenstar L-8483 and Poem TR-FB manufactured by Riken Vitamin. These release agents can be used alone or in combination of two or more. These release agents may be used alone or as a mixture.

  Although content in particular of a mold release agent is not restrict | limited, 0.05-5 mass parts is preferable per 100 mass parts of all the polyester resins which the resin composition of this invention contains, More preferably, 0.05-3 mass parts, More preferably, it is 0.1-1 mass part. If the amount is less than 0.05 parts by mass, sufficient releasability cannot be exhibited, and if it exceeds 5 parts by mass, the generation of gas increases to deteriorate the mold contamination and fogging performance, and the object of the present invention is achieved. Can not.

  The thermoplastic polyester resin composition of the present invention may contain various additives as long as necessary, as long as the characteristics of the present invention are not impaired. Examples of known additives include colorants such as pigments, heat stabilizers, antioxidants, ultraviolet absorbers, light stabilizers, plasticizers, modifiers, antistatic agents, flame retardants, and dyes. In the thermoplastic polyester resin composition of the present invention, the total of the components (A), (B), (C), (D), (E), and (F) is 85 mass with respect to the entire thermoplastic polyester resin composition. %, Preferably 90% by mass or more, and more preferably 95% by mass or more.

  As a method for producing the thermoplastic polyester resin composition of the present invention, components (A) to (E), and (F) component, (G) component, various stabilizers, pigments and the like are mixed as necessary, It can be manufactured by melt-kneading. As the melt-kneading method, any conventionally known method can be used, and a single screw extruder, a twin screw extruder, a pressure kneader, a Banbury mixer, or the like can be used. Among these, it is preferable to use a twin screw extruder. As general melt kneading conditions, in a twin screw extruder, the cylinder temperature is 220 to 270 ° C., and the kneading time is 2 to 15 minutes.

  The component for light reflectors of the present invention is composed of the thermoplastic polyester resin composition of the present invention, and can be produced by molding the thermoplastic polyester resin composition of the present invention. It does not restrict | limit especially as a shaping | molding method, Well-known methods, such as injection molding, extrusion molding, and blow molding, can be used. Among these, an injection molding method is preferably used from the viewpoint of versatility. In particular, it is preferable to manufacture by a manufacturing method including a step of injecting and molding into a mold in which at least a part of the inner surface is a mirror surface.

  The light reflector of the present invention is formed by directly depositing a light reflective metal layer on at least a part of the surface of the light reflector component of the present invention. It does not restrict | limit especially regarding vapor deposition, A well-known method can be used.

  The light reflector thus obtained is a light reflector component of an automobile headlamp such as a headlamp or a rear lamp. For example, a light reflector used for an extension, a reflector, a housing, or a lighting fixture can be used. Can be mentioned.

  EXAMPLES Hereinafter, the present invention will be described more specifically with reference to examples, but the present invention is not limited to these examples. In addition, the measured value described in the Example is measured by the following method.

(1) Intrinsic viscosity (IV):
An Ubbelohde viscometer was used, and measurement was performed at 30 ° C. using a mixed solvent of phenol / tetrachloroethane (mass ratio 1/1).

(2) Titanium content:
Polybutylene terephthalate was wet-decomposed with high-purity sulfuric acid for electronic industry and high-purity nitric acid for electronic industry, and measured using a high resolution ICP (Inductivery Coupled Plasma) -MS (Mass Spectrometer) (manufactured by ThermoQuest).

(3) Terminal carboxyl group concentration (acid value: eq / ton): 0.5 g of polybutylene terephthalate was dissolved in 25 ml of benzyl alcohol, and titrated using a 0.01 mol / l benzyl alcohol solution of sodium hydroxide. The indicator used was 0.10 g phenolphthalein dissolved in a mixture of 50 mL ethanol and 50 mL water.

(4) Terminal hydroxyl group concentration (OH value)
The OH value of polybutylene terephthalate and polyethylene terephthalate was determined by ¹ H-NMR measurement at a resonance frequency of 500 MHz. The measuring apparatus used was an NMR apparatus AVANCE-500 manufactured by BRUKER, and the measuring solution was prepared as follows.
After dissolving the samples 10mg deuterochloroform / hexafluoroisopropanol = 1/1 (volume ratio) 0.12 ml, heavy chloroform 0.48ml and heavy pyridine 5μl was added, was charged after stirring well, the solution to an NMR tube ¹ 1 H-NMR measurement was performed.
Deuterated chloroform was used as the lock solvent, and the total number of times was 128.
The OH number was determined as follows.
When the peak of chloroform is 7.29 ppm, the peak of 8.10 ppm is the terephthalic acid peak (A) derived from polybutylene terephthalate or polyethylene terephthalate. Further, in the case of polybutylene terephthalate resin, a terminal 1,4-butanediol peak (B) is detected at 3.79 ppm. In the case of polyethylene terephthalate resin, the terminal ethylene glycol peak (C) at 4.03 ppm, and A to C in parentheses were integrated values of each peak, and the OH value was obtained from the following formula.
In the case of PBT resin: (B × 1000000/2) / (A × 220/4) = OH value (eq / ton)
In the case of PET resin: (C × 1000000/2) / (A × 192/4) = OH value (eq / ton)

(5) Filler dispersibility A 100 mm × 100 mm × 2 mm thick flat plate molded product formed using an injection molding machine EC100N (manufactured by Toshiba Machine Co., Ltd.) is cut with a diamond cutter or a glass cutter to produce a cross section, and a cross section SEM The presence or absence of agglomerates was visually determined from photographs.
◎: No agglomerate ○: There is an agglomerate, but it is slight, △: Agglomerates can be scattered, ×: Many agglomerates

(6) Surface appearance (specularity)
Using an injection molding machine EC100N (manufactured by Toshiba Machine Co., Ltd.), a 100 mm × 100 mm × 2 mm thick flat plate molded product was injection molded with a mold having a mirror surface polished by # 6000 file. Molding was carried out at a cylinder temperature of 260 ° C., a mold temperature of 60 ° C., a cycle time of 40 seconds, and a low injection speed at which filler floating easily occurred on the surface. The mirror surface of the molded product was visually evaluated for defects (whitening, rough surface) due to floating of the filler.
A: No whitening or rough surface is observed.
○: Whitening and surface roughness are slightly observed depending on the visual angle, but are practically acceptable.
Δ: Whitening and rough surface are observed.
X: Whitening and surface roughness are extremely noticeable.

(7) Fogging property (HAZE%)
A glass cylinder (φ65 × 80 mm) in which a small piece having a size of about 30 mm × 30 mm was cut out from a molded product molded using an injection molding machine EC100N (manufactured by Toshiba Machine Co., Ltd.), and the bottom was covered with aluminum foil. ) And set on a hot plate (Neo Hot Plate HT-1000, manufactured by ASONE). Further, after the glass tube was covered with a slide glass, heat treatment was performed at a hot plate set temperature of 180 ° C. for 24 hours. As a result of this heat treatment, deposits due to decomposition products sublimated from the resin composition were deposited on the inner wall of the slide glass. The HAZE value (haze degree%) of these slide glasses was measured using a haze meter NDH2000 (manufactured by Nippon Denshoku Industries Co., Ltd.).

(8) Mold Stain Acceleration Test Using an injection molding machine EC100N (manufactured by Toshiba Machine Co., Ltd.), as a mold, it has a continuous molding evaluation mold (outer diameter 30 mm, inner diameter 20 mm, thickness 3 mm), and the flow end is a recess No degassing.) Was performed continuously by a short shot method so that the contents such as oligomers were easily accumulated in the concave portion on the opposite side of the gate portion, and mold contamination was observed. The cylinder temperature at the time of molding was 260 ° C., the mold temperature was 60 ° C., the cycle time was 40 seconds, and the mold contamination after 20 shots was evaluated. Mold stains were photographed with a digital camera and evaluated after grayscale processing to make the color uniform.
(Double-circle): Dirt is not recognized.
A: Almost no dirt is observed.
Δ: Dirt is gently recognized in the center near the concave portion on the opposite side of the gate portion.
X: Dirt in the center near the recess on the opposite side of the gate portion is conspicuous in black with a clear outline.

(9) HDT (Load: 0.45 MPa)
The deflection temperature under load (HDT) was used as an index of heat resistance of the resin composition. A multipurpose test piece of ISO-3167 was molded using an injection molding machine EC100N (manufactured by Toshiba Machine Co., Ltd.), and HDT was measured at a load of 0.45 MPa according to ISO-75. In particular, in light reflector applications requiring heat resistance, if the HDT is 135 ° C. or higher, the resin composition satisfies the heat resistance as a light reflector resin, but if it is 140 ° C. or higher, it is more highly satisfactory. And when it is 145 ° C. or higher, it can be said that it is more highly satisfactory.

The compounding components used in Examples and Comparative Examples are shown below.
(A) polybutylene terephthalate resin;
(A-1) Polybutylene terephthalate resin: IV = 0.82 dl / g, acid value = 10 eq / ton, titanium content 30 ppm
(A-2) Polybutylene terephthalate resin: IV = 1.04 dl / g, acid value = 23 eq / ton, titanium content 40 ppm
(A-3) Polybutylene terephthalate resin: IV = 0.83 dl / g, acid value = 30 eq / ton, titanium content 80 ppm
(B) polyethylene terephthalate resin;
(B-1) Polyethylene terephthalate resin: IV = 0.62 dl / g, acid value = 30 eq / ton

(C) inorganic filler;
(C-1) Light calcium carbonate (silica treatment, average particle size 0.15 μm [electron microscopy]): RK-87BR1F (manufactured by Shiroishi Kogyo Co., Ltd.)
(C-2) Light calcium carbonate (silica / epoxysilane coupling agent treatment, average particle size 0.15 μm [electron microscopy]): RK-92BR3F (manufactured by Shiroishi Kogyo Co., Ltd.)
(C-3) Light calcium carbonate (silica / alkylsilane coupling agent treatment, average particle size 1.0 μm [electron microscopy]): RK-82BR1F (manufactured by Shiroishi Kogyo Co., Ltd.)
(C-4) Light calcium carbonate (neutralization treatment with acid, average particle size 0.15 μm [electron microscopy]): RK-75NC (manufactured by Shiroishi Kogyo Co., Ltd.)
(C-5) Light calcium carbonate (fatty acid treatment, average particle size 0.15 μm [electron microscopy]): Vigot-10 (manufactured by Shiroishi Kogyo Co., Ltd.)
(C-6) Light calcium carbonate (no surface treatment, average particle size 0.15 μm [electron microscopy]): Brilliant-1500 (manufactured by Shiroishi Kogyo Co., Ltd.)
(C-7) Light calcium carbonate (no surface treatment, average particle size 0.04 μm [electron microscopy]): NPCC-201 (manufactured by Nagase Sangyo Co., Ltd.)
(C-8) Heavy calcium carbonate (no surface treatment, average particle size: 4.2 μm [laser diffraction method, particle size distribution 50%]): KS-1000 (manufactured by Hayashi Kasei Co., Ltd.)
(C-9) Light calcium carbonate (silane coupling treatment, average particle size 3.0 μm [electron microscopy]): SL-101 (manufactured by Shiroishi Kogyo Co., Ltd.)
(C-10) Titanium dioxide (no surface treatment, average particle size: 0.25 μm [electron microscopy]): PF-739 (Ishihara Sangyo Co., Ltd.)

(D) Kaolin:
(D-1) Hydrous kaolin (no surface treatment, average particle size 0.4 μm [X-ray transmission precipitation method, particle size distribution 50%]): ASP-200 (manufactured by BASF)
(D-2) Hydrous kaolin (no surface treatment, average particle size 0.2 μm [X-ray transmission precipitation method, particle size distribution 50%]): ASP-G90 (manufactured by BASF)
(D-3) calcined kaolin (no surface treatment, average particle size 1.4 μm [X-ray transmission precipitation method, particle size distribution 50%]): SAINTONE-W (manufactured by BASF)
(D-4) Hydrous kaolin (no surface treatment, average particle size 3.5 μm [X-ray transmission precipitation method, particle size distribution 50%]): ASP-400P (manufactured by BASF)

(E) a polyfunctional glycidyl group-containing styrene acrylic polymer;
(E-1) ARUFON UG-4050 (manufactured by Toa Gosei Co., Ltd., Mw: 8500, epoxy value 0.67 meq / g, refractive index 1.55)
(E-2) ARUFON UG-4070 (manufactured by Toa Gosei Co., Ltd., Mw: 9700, epoxy value 1.4 meq / g, refractive index 1.57)
(F) a phosphorus compound;
(F-1) ADK STAB PEP-36 (manufactured by ADEKA)
(F-2) ADK STAB CDA-6 (manufactured by ADEKA)

Release agent:
Triglycerin flubehenate: Poem TR-FB (manufactured by Riken Vitamin Co.)
Stabilizer:
Antioxidant: Irganox 1010 (BASF)

[Examples 1-15, Comparative Examples 1-11]
The same direction in which 0.3 parts by mass of Poem TR-FB as a release agent and 0.2 parts by mass of Irganox 1010 as an antioxidant were added to the ingredients shown in Tables 1 and 2 and the cylinder temperature was set to 260 ° C. Melt kneading was performed with a twin screw extruder, and the obtained strand was cooled with water and pelletized. Each of the obtained pellets was dried at 130 ° C. for 4 hours and used for each of the above-described evaluation tests. The results are shown in Tables 1 and 2.

  The thermoplastic polyester resin compositions of the examples are not only excellent in the surface appearance of the molded product by suppressing the aggregation of calcium carbonate fine particles, but also have good heat resistance due to the use of kaolin, and exhibit low fogging properties and gold. Mold contamination is suppressed.

  On the other hand, the thermoplastic polyester resin composition of the comparative example is incompatible with surface smoothness, mold stain suppression effect and heat resistance. In Comparative Example 1, the surface treatment is not performed on the calcium carbonate particles, the aggregation of calcium carbonate is remarkable, and the surface appearance of the molded product is impaired. In Comparative Example 2, the particle diameter of calcium carbonate is extremely small, and the aggregation of calcium carbonate is remarkable, the surface appearance of the molded product is impaired, and the heat resistance is also low. These calcium carbonates are inferior in dispersibility and give shear heat to the resin during melt-kneading to promote the decomposition of the resin, so that mold contamination increases. In Comparative Examples 3 and 4, the particle size of calcium carbonate is too large regardless of the presence or absence of the surface treatment, and the surface appearance of the molded product is impaired. In Comparative Example 5, the dispersibility of titanium dioxide is good, but the resin is decomposed and inferior in terms of fogging and mold contamination.

  In Comparative Example 6, the dispersibility of kaolin is not as good as that of calcium carbonate, and the surface appearance of the molded product is lost. Moreover, in the comparative example 7, it is only calcium carbonate and heat resistance is not enough. In Comparative Example 8. Although the amount of the inorganic filler added is large and the heat resistance is improved, the surface appearance of the molded product is impaired, and mold contamination and fogging are deteriorated. In Comparative Example 9, the particle diameter of kaolin is large and the surface appearance is deteriorated. In Comparative Example 10, there is no addition of the polyfunctional glycidyl group-containing styrene acrylic polymer (E), and fogging properties and mold contamination cannot be suppressed. Further, in Comparative Example 11, the addition of the polyfunctional glycidyl group-containing styrene acrylic polymer (E) is too much, the resin thickening is remarkable, the appearance of the molded product is deteriorated, and the influence of shearing on the fluid resin during molding is large. As a result, gas increases and mold contamination cannot be suppressed.

  The thermoplastic polyester resin composition of the present invention can suppress mold fouling due to continuous molding, and can provide a highly heat-resistant molded product with high direct metal vapor deposition properties, such as automotive lamps (for example, headlamps). It is suitable for manufacturing light reflectors such as light reflectors (specifically, extensions, reflectors, housings, etc.) and lighting fixtures.

Claims (10)

  A resin composition containing 100 to 50 parts by mass of a polybutylene terephthalate resin (A) and 0 to 50 parts by mass of a polyethylene terephthalate resin (B), and is subjected to a surface treatment having an average particle diameter of 0.05 to 2 μm. 100% polyester resin containing calcium carbonate (C), kaolin (D) having an average particle diameter of 0.05 to 2 μm, and polyfunctional glycidyl group-containing styrenic polymer (E). A thermoplastic polyester resin composition in which the sum of the contents of (C) and (D) is 1 to 20 parts by mass and the content of (E) is 0.05 to 3 parts by mass per part by mass.   2. The thermoplastic polyester resin according to claim 1, wherein the surface treatment of the component (C) is one or more selected from silica treatment, epoxy silane coupling agent treatment, and alkyl silane coupling agent treatment. Composition.   The surface treatment of the component (C) is any one of silica treatment, composite treatment of silica treatment and epoxysilane coupling agent treatment, and composite treatment of silica treatment and alkylsilane coupling agent treatment. A thermoplastic polyester resin composition.   The thermoplastic polyester resin composition according to any one of claims 1 to 3, comprising 0.01 to 5 parts by mass of a phosphorus compound (F) per 100 parts by mass of the total polyester resin.   The component for light reflectors which consists of a thermoplastic polyester resin composition in any one of Claims 1-4.   The light reflector in which the light reflection metal layer is directly formed in at least one part of the surface of the components for light reflectors of Claim 5.   The manufacturing method of the components for light reflectors including the process of inject | pouring and molding the thermoplastic polyester resin composition in any one of Claims 1-4 in the metal mold | die in which at least one part of an inner surface is a mirror surface.   At least polybutylene terephthalate resin (A), polyethylene terephthalate resin (B), surface-treated calcium carbonate (C) having an average particle size of 0.05 to 2 μm, and average particle size of 0.05 to 2 μm A method for producing a thermoplastic polyester resin composition comprising a step of melt-kneading kaolin (D) and a polyfunctional glycidyl group-containing styrenic polymer (E), wherein the blending ratio of (B) is 100 to 50 (B) 0 to 50 parts by mass with respect to parts by mass, and the mixing ratio of (C), (D) and (E) is (C) and (C) per 100 parts by mass of the total polyester resin contained in the resin composition. The manufacturing method of the thermoplastic polyester resin composition in any one of Claims 1-4 whose sum total of D) is 1-20 mass parts and (E) 0.05-3 mass parts.   The method for producing a thermoplastic polyester resin composition according to claim 8, wherein a polybutylene terephthalate resin having a titanium atom content of 60 ppm or less is used as the polybutylene terephthalate resin (A).   The method for producing a thermoplastic polyester resin composition according to claim 8 or 9, wherein a polyethylene terephthalate resin having an acid value of 30 eq / ton or less is used as the polyethylene terephthalate resin (B).