JP2018123256A - Polyester resin composition, and component for light reflection body and light reflection body containing the same - Google Patents

Abstract

PROBLEM TO BE SOLVED: To have low gas properties and greatly suppress mold dirt at the time of continuous molding.SOLUTION: A polyester resin composition contains a polyester resin A containing 70-100 mass% of a polybutylene telephthalate resin and 0-30 mass% of a polyethylene telephthalate resin, contains metal organic acid salt B being either or both of an organic acid salt of alkali metal and an organic acid salt of alkali earth metal, a predetermined amount of a carboxylic acid reactive group-containing compound C and a predetermined amount of a styrenic resin D, where the polyester resin composition contains a predetermined amount of either or both of the alkali metal atom and the alkali earth metal atom with respect to 100 pts.mass of the polyester resin A, and a content of a linear oligomer of the polybutylene telephthalate or contents of a linear oligomer of the polybutylene telephthalate and a linear oligomer of the polyethylene telephthalate is 1,000 mg/kg or less.SELECTED DRAWING: None

Description

  The present invention relates to a polyester resin composition, a component for a light reflector containing the same, and a light reflector.

  Polybutylene terephthalate resin has excellent properties such as injection moldability, mechanical properties, heat resistance, electrical properties and chemical resistance, and is an injection molded product in the fields of automotive parts, mechanical parts, electrical parts and communication parts. Widely used. Further, since it is excellent in mold transferability, it is also used as a lamp member applied to an extension of an automobile or the like that requires a particularly good appearance.

  However, if the polybutylene terephthalate resin is continuously molded, various gases (hereinafter also referred to as “outgas”) are generated during molding, and oligomers of polybutylene terephthalate adhere to the mold and remain. It is known that it becomes mold dirt. This mold contamination may impair the appearance of the molded product. Therefore, it constitutes parts for automobile lamps, other lighting fixtures, etc. that require high luminance appearance (smoothness) and uniform reflectivity, and parts for light reflectors that have a light reflection layer on the surface. Therefore, when a conventional polybutylene terephthalate resin is used, it is necessary to frequently clean the mold during continuous molding. Since the production must be suspended in order to clean the mold, the productivity is adversely affected. For this reason, a polybutylene terephthalate resin capable of suppressing mold contamination is desired.

JP 2014-028883 A JP 2004-323837 A

As a method of suppressing the generation of the outgas, a method of deactivating a catalyst using phenylsulfonic acid has been proposed in Japanese Patent Application Laid-Open No. 2014-028883 (Patent Document 1) and the like, and its reduction effect has been recognized. However, since there is no description regarding the reduction of the oligomer of the polybutylene terephthalate resin, there is room for improvement with respect to suppressing mold contamination. JP-A-2004-323837 (Patent Document 2) describes the reduction of cyclic oligomers such as cyclic dimers and cyclic trimers, but there is no description of linear oligomers as described later. In addition, it was insufficient to suppress mold contamination.
On the other hand, the bleed-out in which the oligomer component and the release agent component derived from the polyester resin are raised on the surface of the molded product may be a problem, and in addition to the low gas property and the low fogging property, the low bleed-out property is required. There are many things.

As a result of intensive studies to suppress mold contamination during continuous molding, the present inventors have found that the root cause of accumulation of mold contamination by continuous molding is the conventionally known cyclic dimer. The present invention has been found out that it is not a cyclic oligomer such as a cyclic trimer but a linear oligomer. Furthermore, the present inventors have found that an improvement effect is exhibited with respect to mold contamination and fogging by obtaining low gas properties that reduce outgas generated during molding, and the present invention has been completed.
Furthermore, it has succeeded in improving the low bleed out property while maintaining the low gas property and the low fogging property.

  That is, the present invention provides a polyester resin composition having low gas properties, capable of greatly suppressing mold contamination during continuous molding, and exhibiting low fogging properties and low bleed out properties, and a light reflector including the same. It is an object to provide a component and a light reflector.

According to the present inventors' previous studies, a polyester resin composition comprising a polyester resin and an alkali metal salt of an alkali metal, a carboxylic acid reactive group-containing compound, and the like, and the polyester resin of the polyester resin composition By making the content of the linear oligomer derived from ≦ 1000 mg / kg or less, it is possible to greatly suppress mold contamination during continuous molding.
However, although the low gas property and fogging property are improved in this composition, it has been clarified that bleedout generated due to the application of heat after molding becomes a problem. Bleed-out causes the molded product to whiten or a rainbow pattern to be observed, so that the appearance is remarkably impaired. As a result of further investigation, the present invention has been reached.

That is, the present invention is as follows.
[1] A polyester resin composition containing polyester resin A containing 70 to 100% by mass of polybutylene terephthalate resin and 0 to 30% by mass of polyethylene terephthalate resin, wherein the polyester resin composition is an alkali metal 0.05 to 3 parts by mass of a carboxylic acid reactive group with respect to 100 parts by mass of the metal organic acid salt B which is one or both of the organic acid salt and alkaline earth metal organic acid salt Containing polyester C and 0.5 to 10 parts by mass of styrene-based resin D, the polyester resin composition contains one or both of an alkali metal atom and an alkaline earth metal atom, and 100 parts by mass of polyester resin A. In contrast, the polyester resin composition contains 0.000005 to 0.05 parts by mass, A polyester resin composition, wherein the content of a linear oligomer of butylene terephthalate, or the content of the linear oligomer of polybutylene terephthalate and the linear oligomer of polyethylene terephthalate is 1000 mg / kg or less.
[2] The polyester resin composition contains 0.0005 to 0.05 parts by mass of one or both of the alkali metal atoms and the alkaline earth metal atoms with respect to 100 parts by mass of the polyester resin A. 1] The polyester resin composition described in 1].
[3] The polyester resin composition according to [1] or [2], wherein the polyester resin composition has a titanium atom content of 50 mg / kg or less.
[4] The polyester resin composition according to any one of [1] to [3], wherein the styrene resin D is a styrene-acrylonitrile copolymer.
[5] The polyester resin composition according to any one of [1] to [4], wherein the carboxylic acid reactive group-containing compound C is a polycarbodiimide compound.
[6] The metal species of the metal organic acid salt B is any one of [1] to [5], which is one or more selected from the group consisting of lithium, sodium, potassium, calcium, and magnesium. Polyester resin composition.
[7] The metal organic acid salt B is one or more selected from the group consisting of lithium acetate, sodium acetate, potassium acetate, calcium acetate, magnesium acetate, lithium benzoate, sodium benzoate and potassium benzoate. The polyester resin composition according to any one of [1] to [6].
[8] A light reflector component comprising the polyester resin composition according to any one of [1] to [7].
[9] A light reflector in which a light reflecting metal layer is formed on at least a part of the surface of the light reflector part according to [8].

  According to the present invention, it is possible to provide a polyester resin composition that has low gas properties, can significantly suppress mold contamination during continuous molding, and exhibits low fogging properties and low bleed out properties. .

The present invention is described in detail below.
[Polyester resin composition]
The present invention relates to polybutylene of 70 to 100% by mass (70% by mass or more and 100% by mass or less, and in the present specification, when the numerical range is expressed using “to”, the range includes upper and lower limit numerical values). It is a polyester resin composition containing the polyester resin A containing a terephthalate resin and 0-30 mass% polyethylene terephthalate resin. The polyester resin composition is 0.05 to 3 masses per 100 mass parts of the metal organic acid salt B, which is one or both of the organic acid salt of alkali metal and the organic acid salt of alkaline earth metal, and 100 mass parts of the polyester resin A. Part of the carboxylic acid reactive group-containing compound C and 0.5 to 10 parts by mass of the styrene resin D. Furthermore, the polyester resin composition contains 0.000005 to 0.05 parts by mass of one or both of alkali metal atoms and alkaline earth metal atoms with respect to 100 parts by mass of the polyester resin A. Furthermore, the content of the linear oligomer of polybutylene terephthalate, or the content of the linear oligomer of polybutylene terephthalate and the linear oligomer of polyethylene terephthalate in the polyester resin composition is 1000 mg / kg or less.

  By including the metal organic acid salt B, the polyester resin composition according to the present invention suppresses the generation of outgas during molding [tetrahydrofuran (hereinafter sometimes referred to as “THF”) and the like] It is possible to suppress the cyclic oligomer and linear oligomer contained in the mold from being carried and adhered to the mold by THF, and mold contamination based on these oligomers can be suppressed. In addition, by containing the carboxylic acid-reactive group-containing compound C, outgas (such as free organic acid), cyclic oligomers and linear oligomers generated during molding are captured to achieve low fogging and mold contamination. It can contribute to suppression of the above. By including the styrene resin D, heat is applied after molding, so that the bleed-out phenomenon in which the oligomer component and the release agent component derived from the polyester resin emerge on the surface of the molded product can be suppressed.

  Furthermore, the polyester resin composition can contain a release agent E described later, and addition of an inorganic filler for the purpose of improving heat resistance and rigidity is not excluded. Furthermore, the polyester resin composition can contain various additives as necessary within the range where the effects of the present invention are not impaired. Examples of the additive include a modifier, a heat stabilizer, an antioxidant, an ultraviolet absorber, a light stabilizer, a plasticizer, a modifier, an antistatic agent, a flame retardant, a dye, and a pigment. The polyester resin composition of the present invention comprises a polyester resin A, a metal organic acid salt B, a carboxylic acid reactive group-containing compound C, a styrenic resin D, and a release agent E (however, the release agent E can be mixed arbitrarily). It is preferable to occupy 85% by mass or more, more preferably 90% by mass or more, and still more preferably 95% by mass or more.

  The polyester resin composition according to the present invention has a low gas property, and can greatly suppress mold contamination during continuous molding. Application to a light reflector component provided with a reflective layer is effective.

<Polyester resin A>
In this invention, the polyester resin A contains 70-100 mass% polybutylene terephthalate resin and 0-30 mass% polyethylene terephthalate resin. The polyester resin A does not exclude the inclusion of a third component other than the polybutylene terephthalate resin and the polyethylene terephthalate resin, but is preferably composed of these two components. The polyester resin A in the polyester resin composition is not particularly limited as long as the polyester resin A is a main component, but is preferably 90% by mass or more, and more preferably 92% by mass or more.

(Polybutylene terephthalate resin)
Polybutylene terephthalate resin is a general polycondensation reaction of dicarboxylic acid mainly composed of terephthalic acid or its ester-forming derivative and diol mainly composed of 1,4-butanediol or its ester-forming derivative. It can be obtained by a typical polymerization method. In the polybutylene terephthalate resin, the repeating unit of butylene terephthalate is preferably 80 mol% or more, more preferably 90 mol% or more, further preferably 95 mol% or more, and 100 mol%. Is most preferred.

  The polybutylene terephthalate resin can contain other polymerization components within a range that does not impair the characteristics thereof, for example, about 20% by mass or less. Examples of polybutylene terephthalate resins containing other polymerization components include polybutylene (terephthalate / isophthalate), polybutylene (terephthalate / adipate), polybutylene (terephthalate / sebacate), polybutylene (terephthalate / decane dicarboxylate), polybutylene (terephthalate) / Naphthalate), poly (butylene / ethylene) terephthalate, and the like. These components may be used alone or in combination of two or more.

  The intrinsic viscosity (IV) of the polybutylene terephthalate resin is preferably 0.3 to 1.6 dl / g, more preferably 0.45 to 1.35 dl / g, and 0.5 More preferably, it is -1.2 dl / g, and it is especially suitable that it is 0.55-1.05 dl / g. The polyester resin composition of the present invention has good mechanical properties and moldability when the intrinsic viscosity (IV) of the polybutylene terephthalate resin is 0.3 to 1.6 dl / g. The intrinsic viscosity (IV) is obtained by using a mixed solvent of phenol / tetrachloroethane (mass ratio 1/1) by an Ubbelohde viscometer, a polybutylene terephthalate resin solution having a concentration of 0.4 g / dl at 30 ° C., It is a value determined from the following formula (I) based on ASTM D4603 by measuring the falling seconds with only the mixed solvent.

Intrinsic viscosity (IV) = 0.25 (η _r −1 + 3lnη _r ) / C (I)
In the above formula (I), η _r = η / η ₀ , η is the falling seconds of the polybutylene terephthalate resin solution, η ₀ is the falling seconds of the mixed solvent only, and C is the polybutylene terephthalate resin The concentration of the solution (g / dl).

  Since the terminal carboxyl group of the polybutylene terephthalate resin plays a catalytic role in the hydrolysis reaction of the polymer, the hydrolysis is accelerated as the amount of the terminal carboxyl group increases. For this reason, it is preferable that the density | concentration of this terminal carboxyl group is low. The concentration of the terminal carboxyl group of the polybutylene terephthalate resin 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. is there.

  The terminal carboxyl group concentration (unit: eq / ton) of the polybutylene terephthalate resin is, for example, a predetermined amount of polybutylene terephthalate resin dissolved in benzyl alcohol, and a 0.01 mol / l benzyl alcohol solution of sodium hydroxide is used. Then, it can be measured by titrating. For example, a phenolphthalein solution may be used as the indicator.

  Since the terminal hydroxyl group of the polybutylene terephthalate resin mainly causes back-biting at the time of melting, it serves as a starting point for producing one of outgases, THF, linear oligomers and cyclic oligomers during molding. For this reason, in order to reduce mold contamination, it is preferable to reduce the concentration of the terminal hydroxyl group to suppress back-biting during molding. The terminal hydroxyl group concentration of the polybutylene terephthalate resin 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. .

The concentration (unit: eq / ton) of the terminal hydroxyl group of the polybutylene terephthalate resin is based on the spectrum obtained by, for example, ¹ H-NMR measurement, and the peak value of terephthalic acid derived from polybutylene terephthalate and the terminal 1,4-butanediol. The peak value can be calculated by a predetermined calculation.

(Polyethylene terephthalate resin)
Polyethylene terephthalate resin is produced by a general polymerization method such as polycondensation reaction of dicarboxylic acid mainly composed of terephthalic acid or its ester-forming derivative and diol mainly composed of ethylene glycol or its ester-forming derivative. It is a polymer that can be obtained. In the polyethylene terephthalate resin, the repeating unit of ethylene terephthalate is preferably 80 mol% or more, more preferably 90 mol% or more, further preferably 95 mol% or more, and preferably 100 mol%. Particularly preferred.

  The polyethylene terephthalate resin can contain other polymerization components within a range that does not impair the characteristics, for example, about 20% by mass or less. Examples of polyethylene terephthalate resins containing other polymerization components 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. These components may be used alone or in combination of two or more. By using such a polyethylene terephthalate resin, the molding shrinkage of the polyester resin composition can be controlled in the present invention.

  The intrinsic viscosity (IV) of the polyethylene terephthalate resin is preferably 0.36 to 1.6 dl / g, more preferably 0.45 to 1.35 dl / g, and 0.5 to More preferably, it is 1.2 dl / g, and it is especially suitable that it is 0.55-1.05 dl / g. The polyester resin composition of the present invention has good mechanical properties and moldability when the intrinsic viscosity (IV) of the polyethylene terephthalate resin is 0.36 to 1.6 dl / g. The intrinsic viscosity (IV) may be measured by the same method as the method for measuring the intrinsic viscosity (IV) of the polybutylene terephthalate resin.

  In this invention, the polyester resin A contains 70-100 mass% polybutylene terephthalate resin and 0-30 mass% polyethylene terephthalate resin. The polyester resin A preferably contains 80 to 100% by mass of polybutylene terephthalate resin and 0 to 20% by mass of polyethylene terephthalate resin, and 90 to 100% by mass of polybutylene terephthalate resin and 0 to 10% by mass. % Of polyethylene terephthalate resin is more preferable. By containing the polyethylene terephthalate resin as described above, it becomes possible to control the molding shrinkage of the polyester resin composition. However, if the content of the polyethylene terephthalate resin exceeds 30% by mass, the mold release at the time of injection molding is performed. This is not preferable because the properties deteriorate and the heat resistance of the polyester resin composition decreases.

  The total amount of the polybutylene terephthalate resin and the polyethylene terephthalate resin in the polyester resin A is preferably 80% by mass or more, more preferably 90% by mass or more, and further preferably 95% by mass or more. The total amount of the polybutylene terephthalate resin and the polyethylene terephthalate resin may be 100% by mass.

(Titanium catalyst)
The polybutylene terephthalate resin constituting the present invention can be obtained, for example, by an esterification reaction or a transesterification reaction using 1,4-butanediol and a titanium catalyst of terephthalic acid or dialkyl terephthalate. At this time, the polyester resin composition of the present invention preferably has a titanium atom content of 50 mg / kg or less from the viewpoint of suppressing decomposition due to retention in the cylinder during molding. That is, in the present invention, the content of the titanium catalyst contained in the polyester resin composition is defined by the content of titanium atoms. The content of titanium atoms is more preferably 45 mg / kg or less, still more preferably 40 mg / kg or less, and particularly preferably 35 mg / kg or less. The lower limit of the titanium atom content is preferably 5 mg / kg, more preferably 8 mg / kg, and even more preferably 15 mg / kg. When the content of titanium atoms exceeds 50 mg / kg, the effect of suppressing mold contamination becomes difficult to develop.

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

  As the titanium catalyst, a known titanium compound can be used. Specific examples thereof include tetraalkyl titanates including titanium alkoxides such as tetraethyl titanate, tetraisopropyl titanate, tetra-n-propyl titanate, tetra-n-butyl titanate, partial hydrolysates and titanium chelate compounds, titanium acetate, Titanyl oxalate, titanyl ammonium oxalate, titanyl sodium oxalate, titanyl potassium oxalate, titanyl calcium oxalate, titanyl strontium oxalate, titanyl oxalate, titanium trimellitic acid, titanium sulfate, titanium chloride, titanium halide Decomposition product, titanium oxalate, titanium fluoride, potassium hexafluorotitanate, ammonium hexafluorotitanate, cobalt hexafluorotitanate, manganese hexafluorotitanate, titanium acetyl Titanium complex with acetonate, hydroxy polyvalent carboxylic acid or nitrogen-containing polyvalent carboxylic acid, complex oxide composed of titanium and silicon or zirconium, reaction product of titanium alkoxide and phosphorus compound, titanium alkoxide and aromatic polyvalent carboxylic acid A reaction product of an acid or an acid anhydride thereof and a predetermined phosphorus compound can be used.

  Among them, from the viewpoint of suppressing mold contamination, tetraalkyl titanates including titanium alkoxides such as tetraethyl titanate, tetraisopropyl titanate, tetra-n-propyl titanate, tetra-n-butyl titanate, partial hydrolysates thereof and titanium chelates It is preferable to use any one selected from the group consisting of compounds. Moreover, it is more preferable to use any one selected from the group consisting of tetraisopropyl titanate, tetra-n-propyl titanate, tetra-n-butyl titanate, ethyl acetoacetate chelate and triethanol titanium aminate.

  Tin can be used as a catalyst instead of or in conjunction with titanium. In addition to titanium and tin, magnesium compounds such as magnesium acetate, magnesium hydroxide, magnesium carbonate, magnesium oxide, magnesium alkoxide, magnesium hydrogen phosphate, calcium hydroxide, calcium carbonate, calcium oxide, calcium alkoxide, hydrogen phosphate Calcium compounds such as calcium, antimony compounds such as antimony trioxide, germanium compounds such as germanium dioxide and germanium tetroxide, manganese compounds, zinc compounds, zirconium compounds, cobalt compounds, orthophosphoric acid, phosphorous acid, hypophosphorous acid, Polyphosphoric acid, phosphorus compounds such as esters or metal salts thereof, and reaction aids such as sodium hydroxide may be used. When the compound used as the reaction aid overlaps with the metal organic acid salt B described later, the total amount of the metal organic acid salt B and the reaction aid is within the range allowed as the metal organic acid salt B in the present invention. The content of

(Linear oligomer)
In the present invention, it is considered that the mold contamination during continuous molding can be suppressed for the following reason.

  The polyester resin composition according to the present invention has a polybutylene terephthalate linear oligomer content, or a polybutylene terephthalate linear oligomer content and a polyethylene terephthalate linear oligomer content of 1000 mg / kg or less. In the present invention, since the polybutylene terephthalate resin has the largest proportion in the polyester resin composition, it is preferable to keep the content of the polybutylene terephthalate linear oligomer low. Since the linear oligomer has a lower melting point than the cyclic oligomer and has a low glass transition temperature, it adheres to the mold more easily than the cyclic oligomer. It is considered that the linear oligomer attached to the mold is tacky and plays a role like a binder to promote adhesion of the cyclic oligomer to the mold. For this reason, reducing the content of the linear oligomer contained in the polyester resin composition contributes very effectively to delaying the onset of mold contamination during continuous molding. Therefore, reducing the content of the linear oligomer is extremely important in suppressing mold contamination.

  Thus, in the present invention, it has been found that linear oligomers are the root cause of mold contamination. Tetrahydrofuran is known to be produced by back-biting reaction of the terminal hydroxyl group, etc., and from the outgas measurement described below, it was found that the amount of tetrahydrofuran generated and the degree of mold contamination were positively correlated. . That is, as the amount of tetrahydrofuran generated increases, the degree of mold contamination becomes severe. In this outgas measurement, a sample of 5 mg polyester resin composition was heated at 265 ° C. for 10 minutes, and the generated component was GS / MS (trade name: “TD-20 / QP-2010Ultra”, Inc. The amount of tetrahydrofuran generated was measured by analysis using Shimadzu Corporation. The detection component can be quantified by toluene conversion or the like. The mold contamination can be evaluated by performing an acceleration test described later.

  From the above, the linear oligomer contained in the polyester resin composition is injected out of the resin system at the time of injection molding in a state of being dissolved in tetrahydrofuran generated during molding, and comes into contact with the mold. At this time, tetrahydrofuran having a low boiling point evaporates without remaining in the mold, but the linear oligomer dissolved in tetrahydrofuran is considered to adhere to the mold as it is. Therefore, reducing the amount of tetrahydrofuran used as a medium also reduces linear oligomers from distilling out of the resin system, resulting in a decrease in the amount of linear oligomers attached to the mold. In addition, mold contamination can be suppressed.

  Here, in this specification, when the linear oligomer is a linear oligomer of polybutylene terephthalate, a total of 2 to 13 constituent units derived from terephthalic acid and constituent units derived from 1,4-butanediol are bonded. An oligomer having a linear structure. The linear oligomer refers to an oligomer having a linear structure in which 2 to 13 structural units derived from terephthalic acid and ethylene glycol derived structural units are combined in a case where the linear oligomer is polyethylene terephthalate. The linear oligomer may have a reactive functional group composed of a hydroxyl group or a carboxyl group at both ends, and both ends may be a carboxyl group or a hydroxyl group. In addition, when the cyclic oligomer is a cyclic oligomer of polybutylene terephthalate, it means an oligomer having a cyclic structure in which 4 to 14 structural units derived from terephthalic acid and 1,4-butanediol are combined. In addition, the cyclic oligomer, when it is a polyethylene terephthalate cyclic oligomer, refers to an oligomer having a cyclic structure in which 4 to 14 structural units derived from terephthalic acid and structural units derived from ethylene glycol are combined.

  As described above, the polyester resin composition according to the present invention has a polybutylene terephthalate linear oligomer content, or a polybutylene terephthalate linear oligomer content and a polyethylene terephthalate linear oligomer content of 1000 mg / kg or less. . The content of the linear oligomer is preferably 950 mg / kg or less, more preferably 900 mg / kg or less, still more preferably 800 mg / kg or less, and particularly preferably 700 mg / kg or less. When the content of the linear oligomer exceeds 1000 mg / kg, the effect of suppressing mold contamination becomes insufficient. The lower limit of the content of the linear oligomer is ideally 0 mg / kg. In addition, when both the linear oligomer of polybutylene terephthalate and the linear oligomer of polyethylene terephthalate are included, the content of the linear oligomer is 1000 mg / kg or less.

  On the other hand, the content of the cyclic oligomer may be 9000 mg / kg or less. The content of the cyclic oligomer is preferably 8000 mg / kg or less, more preferably 6000 mg / kg. However, even if the content of the cyclic oligomer is about 6000 mg / kg, if the content of the linear oligomer exceeds 1000 mg / kg, the effect of suppressing mold contamination decreases. If the content of the linear oligomer is 1000 mg / kg or less, the effect of suppressing mold contamination tends to increase as the content of the cyclic oligomer decreases. In this regard, if the content of the linear oligomer is 1000 mg / kg or less, the content of the cyclic oligomer, which has been conventionally considered to be a cause of mold contamination, is allowed relatively flexibly and should be contained up to 9000 mg / kg or less. Can do.

  For the content of the linear oligomer and cyclic oligomer, for example, the polyester resin composition is dissolved in a solvent composed of hexafluoroisopropanol / chloroform = 2/3 (volume ratio) and precipitated by adding chloroform, methanol, or the like. Subsequently, the filtrated supernatant can be dried, dissolved with dimethylformamide, filtered, and the filtrate can be measured by analysis by liquid chromatographic analysis. For example, the linear oligomer content (quantitative value) can be calculated as BHET (bishydroxyethyl terephthalate), and the cyclic oligomer content (quantitative value) can be calculated as polyethylene terephthalate cyclic trimer.

  The method for setting the content of the linear oligomer to 1000 mg / kg or less is not particularly limited as long as the content of the linear oligomer can be set to 1000 mg / kg or less. In the present invention, since the proportion of the polybutylene terephthalate resin in the polyester resin composition is high, it is effective to reduce the content of the linear oligomer of polybutylene terephthalate.

  Examples of the method for adjusting the content of the linear oligomer to 1000 mg / kg or less include a method of adjusting with a titanium catalyst and a reaction aid, a method of solid-phase polymerization, and a method of extracting the linear oligomer with water or a solvent. be able to. The method for setting the content of the cyclic oligomer to 9000 mg / kg or less is not particularly limited. For example, a method for adjusting the temperature, time, polymerization catalyst, etc. when polymerizing polybutylene terephthalate resin, a method for solid-phase polymerization, a polymerization Examples thereof include a method of performing a heat treatment in a molten state later, a method of extracting a cyclic oligomer using a predetermined solvent, and the like. Moreover, these methods and other methods can be combined to reduce both linear oligomers and cyclic oligomers.

  For example, in the method of solid-phase polymerization of polybutylene terephthalate resin, both the terminal carboxyl group concentration and the terminal hydroxyl group concentration tend to decrease due to the progress of esterification or transesterification. In this method, since the molecular weight increases, it is necessary to adjust the intrinsic viscosity (IV) before solid-phase polymerization and to adjust the temperature and time of solid-phase polymerization.

  In addition, when a polyethylene terephthalate resin is included in the polyester resin composition, suppressing the content of the linear oligomer of polyethylene terephthalate to a low level can also contribute to suppressing mold contamination. The method for reducing the amount of tetrahydrofuran generated will be described in detail below.

<Metallic organic acid salt B>
The polyester resin composition according to the present invention includes a metal organic acid salt B that is one or both of an organic acid salt of an alkali metal and an organic acid salt of an alkaline earth metal. The content is specified based on the content of one or both of alkali metal atoms and alkaline earth metal atoms. Specifically, the content of either one or both of alkali metal atoms and alkaline earth metal atoms is determined. And 0.000005 to 0.05 parts by mass with respect to 100 parts by mass of the polyester resin A. That is, in the present invention, the content of the metal organic acid salt B contained in the polyester resin composition is grasped by specifying the content of either one or both of an alkali metal atom and an alkaline earth metal atom. .

  Here, the reason why the content of the metal organic acid salt B contained in the polyester resin composition is grasped by specifying the content of one or both of an alkali metal atom and an alkaline earth metal atom is as follows. It is as follows. That is, the metal organic acid salt B is considered to exist in a state where the metal ions are dissociated in the polyester resin composition. Therefore, in order to know the content of the metal organic acid salt B, the metal (ion) and the organic acid ( It is necessary to quantify either one or both of (ion). However, organic acids tend to volatilize and are often similar in structure to polymers such as polybutylene terephthalate, which often makes quantification difficult. On the other hand, metal atoms (alkali metal atoms and alkaline earth metal atoms) are relatively likely to remain in the polyester resin composition, and are easily quantified. Therefore, the content of the metal organic acid salt B in the polyester resin composition is grasped by specifying the content of one or both of alkali metal atoms and alkaline earth metal atoms. For these reasons, it is clear that either one or both of the alkali metal atoms and alkaline earth metal atoms are derived from the metal organic acid salt B.

  The content of alkali metal atoms and alkaline earth metal atoms in the polyester resin composition can be measured by ICP emission analysis.

  In other words, in the polyester resin composition according to the present invention, 0.05 kg or more and 500 mg or less (hereinafter referred to as “mg”) of one or both of an alkali metal atom and an alkaline earth metal atom per 1 kg of the mass of the polyester resin A. / Kg "). Further, when the metal organic acid salt B contains both an alkali metal organic acid salt and an alkaline earth metal organic acid salt, both the alkali metal atom and the alkaline earth metal atom are based on 100 parts by mass of the polyester resin A. , 0.000005 to 0.05 parts by mass.

  With the metal organic acid salt B, it is possible to reduce the back-biting reaction at the time of molding the terminal hydroxyl group of the polybutylene terephthalate resin, and the amount of THF generated can be reduced. When one or both of alkali metal atoms and alkaline earth metal atoms derived from the metal organic acid salt B is less than 0.000005 parts by mass (0.05 mg / kg) with respect to 100 parts by mass of the polyester resin A In addition, the metal organic acid salt B is less likely to exert an effect of suppressing mold contamination. Moreover, when one or both of an alkali metal atom and an alkaline-earth metal atom exceeds 0.05 mass part (500 mg / kg) with respect to 100 mass parts of polyester resin A, decomposition | disassembly of a polyester resin composition is accelerated | stimulated. , Mold dirt and fogging may be deteriorated.

  Furthermore, it is preferable that a polyester resin composition contains 0.0005-0.05 mass part of any one or both of an alkali metal atom and an alkaline-earth metal atom with respect to 100 mass parts of said polyester resins A. This numerical range is more preferably 0.0005 to 0.04 parts by mass (5-400 mg / kg), still more preferably 0.0006 to 0.03 parts by mass (6 to 300 mg / kg). Preferably it is 0.0007-0.02 mass part (7-200 mg / kg).

  The metal species of the metal organic acid salt B that can be used in the polyester resin composition of the present invention is one or more selected from the group consisting of lithium, sodium, potassium, calcium, and magnesium from the viewpoint of mold contamination. Is preferred. Of these, lithium, sodium and potassium are preferable, and potassium is most preferable.

  Specific examples of the alkali metal or alkaline earth metal salt include saturated aliphatic carboxylates such as formic acid, acetic acid, propionic acid, butyric acid, and oxalic acid, and unsaturated aliphatic carboxylates such as acrylic acid and methacrylic acid. Acid salts, aromatic carboxylates such as benzoic acid, halogen-containing carboxylates such as trichloroacetic acid, hydroxycarboxylic acid salts such as lactic acid, citric acid, salicylic acid and gluconic acid, 1-propanesulfonic acid, 1-pentanesulfonic acid And organic sulfonates such as naphthalene sulfonic acid, organic sulfates such as lauryl sulfate, and carbonates. In addition, although carbonate is normally taken as an inorganic acid salt, in this invention, the acid which has carbon is regarded as an organic acid, and carbonate is included in the range of organic acid salt.

  From the viewpoint of suppressing mold stains and handling properties, the metal organic acid salt B is composed of lithium acetate, sodium acetate, potassium acetate, calcium acetate, magnesium acetate, lithium benzoate, sodium benzoate and potassium benzoate. It is preferable that it is 1 type or 2 types or more selected from more. Especially, it is more preferable that it is 1 type, or 2 or more types chosen from the group which consists of lithium acetate, sodium acetate, potassium acetate, calcium acetate, and magnesium acetate, and potassium acetate is especially preferable. In addition, these metal organic acid salt B may be used individually by 1 type, and may use 2 or more types together.

  The method for containing the metal organic acid salt B in the polyester resin composition is not particularly limited. For example, a method of adding at the initial stage of polymerization of the polybutylene terephthalate resin constituting the polyester resin A (after the esterification reaction or after the transesterification reaction), the latter stage of polymerization of the polybutylene terephthalate resin (during the polycondensation step (decompression step), or completion of the polymerization After), a method of adhering to the pellet surface after being pelletized, or a method of infiltrating into the pellet, or a master pellet containing a high concentration of metal organic acid salt B is produced in advance, and the master pellet is polyester A method of mixing at the time of melt kneading to obtain a resin composition can be employed. Furthermore, a method of adding a master pellet containing the metal organic acid salt B at a high concentration when forming into a molded body may be used. The above-mentioned initial polymerization stage and late polymerization stage of the polybutylene terephthalate resin refer to the initial polymerization stage and the late polymerization stage in the so-called melt polymerization of the polybutylene terephthalate resin.

  When the metal organic acid salt B is included when producing the polybutylene terephthalate resin, a part of the metal organic acid salt B may be removed from the reaction system under reduced pressure conditions with respect to the amount added. For this reason, the amount of metal organic acid salt B added is determined based on the reaction apparatus used, conditions, etc., and if necessary, the metal organic acid salt B remaining in the polyester resin composition by several trials (ie, alkali metal) It is necessary to determine the amount of atoms and / or alkaline earth metal atoms). In addition, when the polyester resin composition of the present invention is produced by kneading using a twin screw extruder or the like, the same thing may occur when venting (depressurizing), so take necessary measures. It is necessary to determine the amount of metal organic acid salt B added.

  In particular, in the present invention, either one or both of an alkali metal atom and an alkaline earth metal atom derived from the metal organic acid salt B is 0.0005 to 0.05 parts by mass (5 to 100 parts by mass of the polyester resin A). When the polyester resin composition is constituted so as to include 500 mg / kg), the polyester resin composition is preferably obtained by using master pellets containing the metal organic acid salt B at a high concentration. The base resin of the master pellet is preferably one of the resins constituting the polyester resin composition, and more preferably a polybutylene terephthalate resin having the largest proportion in the polyester resin composition. The master pellet containing the metal organic acid salt B at a high concentration can be produced by mixing the base resin and the metal organic acid salt B, and melt-kneading them. The melt kneading method may be a known method, 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.

  The content of the metal organic acid salt B in the master pellet is also specified on the basis of the content of one or both of the alkali metal atom and the alkaline earth metal atom. It is preferable that any one or both of metal atoms are 0.02-1.5 mass parts (200-15000 mg / kg) with respect to 100 mass parts of said master pellets. If the content in the master pellet exceeds 1.5 parts by mass, the base resin is decomposed during the production of the master pellet, which may adversely affect the inclusion in the polyester resin composition. When the content in the master pellet is less than 0.02 parts by mass, the content of the metal organic acid salt B as the master pellet is small, and the productivity is not good.

  The reason why these metal organic acid salts B have an effect of suppressing mold contamination is presumed to be as follows. That is, the metal organic acid salt B suppresses the hydrolysis reaction of the polybutylene terephthalate resin and the back-biting reaction of the terminal hydroxyl group due to the effect of stabilizing the ester group or the so-called buffer effect. Thereby, the production | generation of tetrahydrofuran can mainly be suppressed. Therefore, the polyester resin composition according to the present invention can obtain a low gas property and a significant effect of suppressing mold contamination.

When the polyester resin composition according to the present invention contains the metal organic acid salt B, the Color-b value by the L ^* a ^* b ^* color system increases and the yellowishness tends to increase. From the viewpoint of color blur at the time of coloration, the Color-b value of the polyester resin composition is preferably suppressed to 6 or less. Here, the method of adding the metal organic acid salt B by the master pellet is preferable because the Color-b value tends to be lower than the method of adding the metal organic acid salt B during the polymerization of the polybutylene terephthalate resin. The Color-b value of the polyester resin composition is more preferably 5 or less, and even more preferably 4 or less.

  The Color-b value is, for example, a commercially available precision spectrophotometric colorimeter with respect to the mirror surface of a flat plate (molded using a mold having a mirror surface) having a mirror surface on one side obtained by injection molding a polyester resin composition. It can obtain by measuring based on JISZ8722: 2009 and JISZ8781-4: 2013 using etc.

<Carboxylic acid reactive group containing compound C>
The polyester resin composition according to the present invention includes 0.05 to 3 parts by mass of the carboxylic acid reactive group-containing compound C with respect to 100 parts by mass of the polyester resin A. By setting the content of the carboxylic acid reactive group-containing compound C in such a range, a gas component such as a free acid generated from the release agent E described later, a cyclic oligomer, a linear oligomer, and polybutylene terephthalate and polyethylene The terephthalate monomer and the like can be efficiently captured, and excellent low gasity including low fogging can be realized. Contributes to the suppression of mold contamination.

  If the carboxylic acid reactive group-containing compound C exceeds 3 parts by mass, gelation occurs due to the reaction with the polyester resin A, which is not preferable. In addition, when the carboxylic acid reactive group-containing compound C is less than 0.05 parts by mass, the above-described capturing is not efficiently performed and the effect obtained is insufficient, which is not preferable. The compounding amount of the carboxylic acid reactive group-containing compound C is preferably 0.06 to 2 parts by mass and more preferably 0.07 to 1 part by mass with respect to 100 parts by mass of the polyester resin A.

  In the present invention, the carboxylic acid reactive group-containing compound C refers to a compound containing one or more carboxylic acid reactive groups in one molecule. Due to the action of the carboxylic acid reactive group, the carboxylic acid reactive group-containing compound C is a free fatty acid resulting from the decomposition of the fatty acid ester compound contained in the mold release agent E described later, and a free carboxylic acid generated during heat treatment or high temperature use. Etc. can be captured immediately and the volatilization amount of these free acids can be reduced. Since these free acids are gas components generated from the polyester resin composition and a molded product produced from the polyester resin composition, the trapping thereof is effective for realizing low gas properties. In particular, free carboxylic acid, which is a kind of free acid, is known to volatilize at a relatively low temperature, and volatiles often crystallize and cause fogging.

  The carboxylic acid reactive group refers to a functional group that reacts with carboxylic acid. Examples of the carboxylic acid reactive group include a glycidyl group, an oxazoline group, an oxetane group, and a carbodiimide group. Among these, a carbodiimide group is preferable as a functional group for reacting with a carboxylic acid because the reaction is quicker than a glycidyl group, an oxazoline group, and an oxetane group. Furthermore, the carbodiimide group is superior to the glycidyl group, oxazoline group, and oxetane group in that coexistence with a hydroxyl group-reactive group described later does not become a problem. Moreover, the carbodiimide group is preferable because a compound having the carbodiimide group is less likely to volatilize. The carbodiimide group can capture the gas component by addition reaction with the gas component described above. Cyclic oligomers, linear oligomers and the above monomers can also be captured by addition reaction with carbodiimide groups.

  In addition to the carboxylic acid reactive group, the carboxylic acid reactive group-containing compound C preferably contains one or more hydroxyl reactive groups in one molecule. The hydroxyl group-reactive group refers to a functional group that reacts with a hydroxyl group. By the action of the hydroxyl-reactive group, the free hydroxyl group-containing compound resulting from the decomposition of the fatty acid ester compound contained in the release agent E, which will be described later, and the free hydroxyl group-containing compound generated at the time of heat treatment or high temperature use are captured. Volatilization amount can be reduced. The hydroxyl group reactive group is a reactive group different from the carboxylic acid reactive group, and examples thereof include an isocyanate group and an acid anhydride group. The hydroxyl-reactive group is preferably an isocyanate group from the viewpoint of reactivity. As mentioned above, it is preferable that the carboxylic acid reactive group containing compound C in this invention is a compound which each contains 1 or more carbodiimide group and isocyanate group in 1 molecule.

  The advantage of the carboxylic acid-reactive group-containing compound C containing one or more carbodiimide groups and isocyanate groups in one molecule can be said also about the following points. That is, these reactive groups can easily react not only with a free hydroxyl group-containing compound and a free acid but also with a thermoplastic resin. For example, a thermoplastic resin having a large molecular weight and a fatty acid ester decomposition product (free fatty acid, free hydroxyl group-containing compound, etc.) are bonded via a carboxylic acid reactive group-containing compound C, thereby The volatilization amount of the decomposition product can be greatly reduced. At the same time, a thermoplastic resin and a hydrolyzate (linear oligomer, cyclic oligomer, etc.) of this thermoplastic resin are bonded via a carboxylic acid reactive group-containing compound C, so that the free hydrolyzate is greatly reduced. Can be reduced.

  Further, in the case of a thermoplastic polyester resin containing a carboxyl group as in the present invention, a carboxylic acid-reactive group-containing compound C containing a carbodiimide group is added to block the terminal carboxyl group (of the proton derived from the carboxyl group). By preventing the formation), the hydrolysis reaction can be suppressed very effectively, and further effects such as improved processability as a resin composition can be provided.

  Furthermore, the carboxylic acid reactive group-containing compound C in the present invention is preferably a polycarbodiimide compound having two or more structures of -N = C = N- in one molecule. As such a polycarbodiimide compound, a known polycarbodiimide compound produced by a carbon dioxide removal reaction of a diisocyanate compound can be exemplified. For example, U.S. Pat. No. 2,941,956, Japanese Patent Publication No. 47-003279, "J. Org. Chem., 28, 2069-2075 (1963)", and "Chemical Review 1981, Vol. 81, No. 4,619". -621 "and the like.

  Examples of the diisocyanate compound used as a raw material for the polycarbodiimide compound include aliphatic or alicyclic isocyanate compounds such as hexamethylene diisocyanate, dicyclohexylmethane diisocyanate, cyclohexane-1,4-diisocyanate, isophorone diisocyanate, and methylcyclohexane diisocyanate, and 4,4-diphenylmethane. Diisocyanate, 4,4-diphenyldimethylmethane diisocyanate, 1,3-phenylene diisocyanate, 1,4-phenylene diisocyanate, 2,4-tolylene diisocyanate, 2,6-tolylene diisocyanate, 1,5-naphthylene diisocyanate, xylylene Range isocyanate, tetramethylxylylene diisocyanate, 1,3,5-triisopropylphenylene Aromatic isocyanate compounds such as 2,4-diisocyanate and the like. By reacting one or more of these compounds, a polycarbodiimide compound that can be preferably used as the carboxylic acid reactive group-containing compound C can be produced.

  The carboxylic acid reactive group-containing compound C may have a branched structure. For example, a branched structure can be formed by introducing a functional group other than a carbodiimide group and an isocyanate group. Furthermore, when the carboxylic acid reactive group-containing compound C includes an isocyanate group, it is preferable that a part or all of the terminal isocyanate group is blocked. As end-capping agents, monoisocyanate compounds such as phenyl isocyanate, tris isocyanate, dimethylphenyl isocyanate, cyclohexyl isocyanate, butyl isocyanate, naphthyl isocyanate, and -OH group, -COOH group, -SH group, -NHR group (where R is A compound having a hydrogen atom or an alkyl group) can be used.

  An advantage of blocking part or all of the terminal isocyanate group is that the reaction in the polyester resin composition can be controlled. For example, the degree of polymerization and melt viscosity can be controlled. When a certain amount or more of the carboxylic acid reactive group-containing compound C in which the terminal isocyanate group is not blocked is added to the polyester resin A, the melt viscosity is remarkably increased due to thickening, so that the addition amount is limited. When the addition amount is limited, there is a possibility that the low gas property and the mold stain suppressing effect due to the addition of the carboxylic acid reactive group-containing compound C cannot be obtained as desired. In such a case, the above problem can be solved by using the carboxylic acid reactive group-containing compound C in which a part or all of the terminal isocyanate groups are blocked. Even when all of the terminal isocyanate groups are blocked, the carboxylic acid-reactive group-containing compound C can efficiently capture the free carboxylic acid based on the high reactivity of the carbodiimide group. Therefore, sufficient low gas property can be acquired.

  Commercially available products that can be used as the carboxylic acid reactive group-containing compound C are listed below. Aromatic polycarbodiimide compounds (trade names: “STABAKZOL P”, “STABAKZOL P100”, “STABAKZOL P400”, etc., manufactured by Rhein Chemie), aliphatic polycarbodiimide compounds (trade name: “Carbodilite LA-1” ”,“ Carbodilite HMV-8CA ”,“ Carbodilite HMV-15CA ”, etc., manufactured by Nisshinbo Chemical Co., Ltd., carbodiimide-modified diphenylmethane diisocyanate (trade names:“ Cosmonate LK ”,“ Cosmonate LL ”, manufactured by Mitsui Chemicals, Inc. Or a brand name: "Lupranato MM-103", BASF INOAC polyurethane make) etc. can be mentioned. Among these, from the viewpoint of affinity with a free acid, it is preferable to use a carboxylic acid reactive group-containing compound C having an aliphatic or alicyclic structure. Among the above commercially available products, the “carbodilite series” is preferable because it has an aliphatic or alicyclic structure. In addition, when the carboxylic acid reactive group-containing compound C is an aromatic polycarbodiimide, the affinity with the free acid may be deteriorated, so that the carbodiimide group and the fatty acid do not efficiently react with each other. May be reduced.

  Here, when a conventional polybutylene terephthalate resin is used to form a polyester resin composition and a molded product obtained by molding the polyester resin composition is applied as a lamp part for an automobile, the headlight cover of the automobile is yellowed due to deterioration over time. The fogging problem of clouding occurred. The polyester resin composition of the present invention can effectively suppress the generation of outgas which causes clouding by the carboxylic acid reactive group-containing compound C, and can have excellent low fogging properties. Specifically, the polyester resin composition of the present invention can solve the above-mentioned fogging problem when the haze value of the glass plate after the fogging test (160 ° C.) is 5% or less. When the haze value of the glass plate after the fogging test exceeds 5%, the above-mentioned fogging problem is practically caused in a headlight cover of an automobile or other lighting fixtures. Furthermore, mold contamination is likely to occur during injection molding, which may adversely affect the quality and productivity of the molded product.

  The fogging test can be performed by the following method. That is, a plurality of small pieces having a size of about 40 mm × 40 mm are cut out from a molded product (thickness 2 mm) obtained by injection molding the polyester resin composition. Next, a total of 10 g of these small pieces is put in a glass tube (for example, φ65 × 80 mm) whose aluminum foil is covered to make the bottom, and this glass tube is set upright on a known hot plate. Further, the glass tube is covered with a slide glass (for example, 78 mm × 76 mm × 1 mm) so that there is no gap, and then heat-treated at 160 ° C. for 24 hours with the hot plate. As a result of the heat treatment, a decomposition product sublimated from the polyester resin composition is deposited on and adhered to the inner wall of the slide glass, and the haze value is measured with respect to the slide glass using a known haze meter or the like. A haze value is calculated | required from the ratio of the diffuse transmission light in all the light transmitted light, and can be used as a parameter | index of cloudiness (%). A smaller haze value (transparent) means that the polyester resin composition has a lower fogging property.

<Styrene resin D>
The polyester resin composition according to the present invention includes 0.5 to 10 parts by mass of styrene resin D with respect to 100 parts by mass of polyester resin A. By setting the content of the styrene resin D in such a range, it is possible to effectively suppress the bleed out of the oligomer component derived from the polyester resin and the release agent E described later.
The carboxylic acid-reactive group-containing compound C functions as an oligomer or a release agent component scavenger, while the styrene resin D is effective for suppressing the release of the release agent and suppressing shrinkage. This is considered because the styrene resin D performs the following actions.
In the polyester resin composition, low molecular weight components such as oligomers and release agents are likely to be present in an amorphous region having a lower molecular chain density. If the crystallization (arrangement / density increase of molecular chains) of the region proceeds due to the application of heat and the molecular mobility of the low molecular weight component itself increases, the low molecular weight component is easily discharged from the region. Thereby, it will be observed as a bleed-out when discharged | emitted to the molded article surface.
On the other hand, when the styrene resin D is dispersed in the polyester resin composition, the low molecular weight component can be present in the styrene resin D that does not crystallize, and the proportion discharged to the surface of the molded product is high. It is considered that the bleed-out is suppressed because of a significant decrease.
As an amorphous resin that can be expected to have the same action (effect) as the styrene resin D, there is polycarbonate. However, when polycarbonate is blended with the polyester resin composition, it may adversely affect the appearance such as whitening when the resulting molded product is heated.

When the styrene-based resin D exceeds 10 parts by mass, the mirror surface appearance of the molded product may be significantly deteriorated due to phase separation from the polyester resin A.
Moreover, there exists a possibility that the bleed-out suppression effect and shrinkage | contraction suppression effect which were mentioned above that styrene-type resin D is less than 0.5 mass part cannot fully be acquired.
The blending amount of the styrene resin D is preferably 1 to 8 parts by mass and more preferably 2 to 6 parts by mass with respect to 100 parts by mass of the polyester resin A.

The Mw of the styrene resin D is preferably more than 50000, and preferably less than 600000 from the viewpoint of moldability. When Mw is 50000 or less, the shrinkage suppression effect may be low. If the Mw is 600,000 or more, the fluidity as the polyester resin composition is lowered, and the moldability may be impaired. The Mw of the styrene resin D is more preferably 60000 or more, further preferably 80000 or more, and particularly preferably 100000 or more. Further, Mw is more preferably 500,000 or less, further preferably 400,000 or less, and particularly preferably 300,000 or less.
Although the styrene resin D exhibits the above-described action (effect), it is important to suppress shrinkage of the resin composition. In order to obtain the shrinkage suppressing effect, the Mw of the styrene resin D is preferably in the above-described range.
Another measure for expressing the molecular weight of the styrene resin D is melt volume flow rate (MVR). The MVR of the styrene resin D is preferably ^{3 to} 100 cm 3/10 min (measurement conditions: 220 ° C., 10 kgf). The reason why this range is preferable is the same as in the case of Mw. MVR of the styrene resin D ^is preferably a 4~50cm 3 / 10min.

  The styrene resin D is not particularly limited as long as it is a styrene resin containing a styrene monomer as a constituent component. The styrene resin D includes a polymer obtained by polymerizing a styrene monomer, a copolymer of a styrene monomer and a monomer copolymerizable with the styrene monomer, and at least in the presence of rubber. Graft copolymers obtained by polymerizing styrene monomers, graft copolymers obtained by polymerizing at least styrene monomers and monomers copolymerizable with styrene monomers in the presence of rubber, etc. Can be mentioned.

Examples of the styrene monomer include styrene, α-methyl styrene, p-methyl styrene, and preferably styrene.
Examples of the monomer copolymerizable with the styrene monomer include (meth) acrylonitrile, (meth) acrylic acid alkyl ester, and the like. In the present invention, “(meth) acrylonitrile” represents “methacrylonitrile” or “acrylonitrile”. Similarly, “(meth) acrylic acid” represents “methacrylic acid” or “acrylic acid”. Examples of the alkyl group of the (meth) acrylic acid alkyl ester include a methyl group, an ethyl group, and a propyl group.
Other monomers that can be copolymerized with the styrenic monomer include maleimide, N-phenylmaleimide, vinyl acetate, vinyl propylate, maleic anhydride, maleic acid monoester, maleic acid diester, and the like. Further, olefins such as ethylene, propylene and 1-butene, and dienes such as butadiene and isoprene can be used.
Examples of rubbers include diene rubbers, acrylic rubbers, ethylene / propylene rubbers, and silicone rubbers. Preferred are diene rubbers and acrylic rubbers, and rubbers having a glass transition temperature of 10 ° C. or lower are more preferable. preferable.

The styrene resin D is preferably a styrene-acrylonitrile copolymer that can further exert the effects of the present invention. Specific examples include acrylonitrile-styrene (AS) copolymer, acrylonitrile-butadiene-styrene (ABS) copolymer, acrylonitrile-ethylene-styrene (AES) copolymer, acrylonitrile-styrene-acrylate (ASA). A copolymer etc. are mentioned preferably, and especially an AS copolymer is preferable. This styrene-acrylonitrile copolymer may be modified with a reactive functional group such as a glycidyl group, a carboxyl group, or an acid anhydride group.
In the styrene resin D, the content of the styrene monomer is preferably 50% by mass or more, and more preferably 60% by mass or more. Although there is no limitation in particular about an upper limit, it is preferable that it is 80 mass% or less.

  Examples of the method for producing the styrene resin D include known methods such as an emulsion polymerization method, a solution polymerization method, a suspension polymerization method, and a bulk polymerization method. Among these, the emulsion polymerization method, the solution polymerization method, and the suspension polymerization method tend to reduce the content of the oligomer of the styrenic resin, and are preferable from the viewpoints of low gas properties and low fogging properties.

<Others>
(Release agent E)
The polyester resin composition of the present invention can contain a release agent E in order to further improve the releasability. The mold release agent E is preferably a fatty acid ester compound from the viewpoint of suppressing mold contamination. The fatty acid ester compound can include a compound in which a carboxylic acid is partially esterified with monoglycol or polyglycol, and a compound in which a metal salt is partially formed. When the release agent E is a fatty acid ester compound, the action of the metal organic acid salt B and the carboxylic acid reactive group-containing compound C tends to suppress the production of free fatty acids based on the release agent E, Mold fouling can be suppressed and fogging properties can be improved. The content of the release agent E is preferably 0.05 to 3 parts by mass with respect to 100 parts by mass of the polyester resin A. If the content of the release agent E is less than 0.05 parts by mass, a sufficient release effect may not be obtained, and a release failure or release wrinkles may occur. The mold release agent E gasifies itself or bleeds out, thereby causing mold contamination. Furthermore, for example, when the polyester resin composition containing the release agent E is applied to an automobile lamp, it adheres to a headlight cover or mirror under a temperature environment in the range of 100 ° C. to 200 ° C. and generates fog ( Fogging). These problems become significant when the content of the release agent E exceeds 3 parts by mass.

(Inorganic filler)
The polyester resin composition according to the present invention can contain an inorganic filler as long as the effects of the present invention are not impaired for the purpose of improving heat resistance and rigidity. It does not specifically limit as a kind of inorganic filler, A well-known thing can be used. The inorganic filler may be surface-treated in order to improve compatibility with the polyester resin composition and dispersibility in the polyester resin composition. From the viewpoint of the surface appearance of the molded article of the polyester resin composition, the average particle diameter of the inorganic filler is preferably 3.0 μm or less. The content of the inorganic filler is preferably less than 1 part by mass with respect to 100 parts by mass of the polyester resin A, more preferably 0.8 parts by mass or less, and further preferably 0.5 parts by mass or less. preferable. When the content of the inorganic filler is 1 part by mass or more, there is a possibility that the request cannot be met when a more sophisticated mirror appearance is required.

<Method for producing polyester resin composition>
The method for producing the polyester resin composition according to the present invention can be produced by mixing the above-described components and additives such as a stabilizer to be added as necessary, and melt-kneading. As a method of melt kneading, a known method can be used. For example, melt kneading can be performed using a single screw extruder, a twin screw extruder, a pressure kneader, a Banbury mixer, or the like. Among these, it is preferable to use a twin screw extruder. As general melt-kneading conditions, when a twin-screw extruder is used, the cylinder temperature can be set to 230 to 270 ° C., and the kneading time can be set to 2 to 15 minutes.

  It does not restrict | limit especially as a shaping | molding method of the polyester resin composition which concerns on this invention, It can shape | mold by well-known methods, such as injection molding, extrusion molding, and blow molding. Among these, it is preferable to use an injection molding method from the viewpoint of versatility.

<Light reflector parts>
The component for light reflectors according to the present invention includes the polyester resin composition. The light reflector part can be obtained by molding a polyester resin composition by a known method such as an injection molding method, an extrusion molding method, or a blow molding method, and is obtained by using an injection molding method from the viewpoint of versatility. It is preferable. The component for a light reflector becomes a light reflector described later, for example, by including a light reflecting metal layer.

<Light reflector>
In the light reflector according to the present invention, a light reflecting metal layer is formed on at least a part of the surface of the light reflector component. For example, the light reflector can be obtained by directly forming a metal thin film (for example, an aluminum foil) as a light reflecting metal layer on at least a part of the surface of the light reflector component. In particular, the light reflector is preferably obtained by depositing a metal thin film on at least a part of the surface of the light reflector component. The vapor deposition method is not particularly limited, and a known method can be used.

  The light reflector according to the present invention includes, for example, automobile lamps (headlights, etc.), light reflectors (extensions, reflectors, housings, etc.), and various parts such as lighting fixtures, electrical parts, electronic parts, household goods, etc. Can be used as

  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 a value measured by the following method.

  (1) Intrinsic Viscosity (IV): The intrinsic viscosity (IV) of the polybutylene terephthalate resin a and the polyethylene terephthalate resin b is mixed with phenol / tetrachloroethane (mass ratio 1/1) using an Ubbelohde viscometer, Measured at 30 ° C. The polybutylene terephthalate resin a solution with a concentration of 0.4 g / dl, the polyethylene terephthalate resin b solution with a concentration of 0.4 g / dl, and the mixed solvent alone at 30 ° C. were measured, and values were obtained from the above formula (I). Asked.

  (2) Terminal carboxyl group concentration (unit: eq / ton, expressed as acid value): 0.5 g of polybutylene terephthalate resin a was dissolved in 25 ml of benzyl alcohol, and a 0.01 mol / l benzyl alcohol solution of sodium hydroxide was dissolved. Used and titrated. The indicator used was a solution in which 0.10 g of phenolphthalein was dissolved in a mixed solution of 50 ml of ethanol and 50 ml of water. The terminal carboxyl group concentration of the polyethylene terephthalate resin b was also quantified by the same method.

(3) Terminal hydroxyl group concentration (unit: eq / ton): The terminal hydroxyl group concentration of the polybutylene terephthalate resin a was quantified by ¹ H-NMR measurement at a resonance frequency of 500 MHz. As the measuring apparatus, an NMR apparatus (trade name: “AVANCE-500”, manufactured by BRUKER) was used.

First, after dissolving polybutylene terephthalate resin a 10 mg or polyethylene terephthalate resin b 10 mg in 0.12 ml of a solvent composed of deuterated chloroform / hexafluoroisopropanol = 1/1 (volume ratio), 0.48 ml of deuterated chloroform and 5 μl of deuterated pyridine were added, The resin solution was prepared by thoroughly stirring. Thereafter, the resin solution was filled in an NMR tube, and ¹ H-NMR measurement was performed. Deuterated chloroform was used as the lock solvent, and the total number of times was 128.

Next, in the measured ¹ H-NMR spectrum, when the peak of chloroform appears at 7.29 ppm, the terephthalic acid peak (i) derived from polybutylene terephthalate or polyethylene terephthalate appears at 8.10 ppm. Furthermore, in the case of the polybutylene terephthalate resin a, a terminal 1,4-butanediol peak (ii) appears at 3.79 ppm. In the case of the polyethylene terephthalate resin b, a terminal ethylene glycol peak (iii) appears at 4.03 ppm. For this reason, the terminal hydroxyl group concentration was calculated | required from the following formula by making (i)-(iii) the integral value of each peak.

In the case of polybutylene terephthalate resin a: {(ii) × 1000000/2} / {(i) × 220/4} = terminal hydroxyl group concentration (eq / ton)
In the case of polyethylene terephthalate resin b: {(iii) × 1000000/2} / {(i) × 192/4} = terminal hydroxyl group concentration (eq / ton).

  (4) Titanium atom content, potassium atom content, magnesium atom content: The polyester resin composition is wet-decomposed with high-purity sulfuric acid for electronic industry and high-purity nitric acid for electronics industry, and ICP (trade name: “SPECTROBLUE”, Ametec Co., Ltd.) was used to measure by an emission analysis method.

  (5) Oligomer content: After dissolving 0.1 g of the polyester resin composition in 3 ml of a solvent consisting of hexafluoroisopropanol / chloroform = 2/3 (volume ratio), 20 ml of chloroform and 10 ml of methanol are added to precipitate the polymer. It was. Subsequently, the filtrated supernatant was dried to solid, then dissolved in 10 ml of dimethylformamide and filtered, and each oligomer component was quantified in the filtrate by a liquid chromatographic analysis method. The quantitative value of the linear oligomer was calculated by BHET (bishydroxyethyl terephthalate) conversion, and the quantitative value of the cyclic oligomer was calculated by polyethylene terephthalate cyclic trimer, using each calibration curve. The measurement was performed under the following conditions.

Liquid chromatograph analyzer: Product name: “Prominence”, manufactured by Shimadzu Corporation Column: Shim-pack XR-ODS 2.2 μm (3 × 100 mm)
Mobile phase: A 0.2% acetic acid aqueous solution, B acetonitrile gradient: 0 min (10% B), 25 min (100% B), 27 min (100% B), 27.01 min (10% B), 32 min (10% B) )
Flow rate: 1.1ml / min
Column temperature: 50 ° C
Injection volume: 5 μl
Detection wavelength: UV258nm.

  (6) Color-b value (flat plate): An injection molding machine (trade name: “EC100N”, manufactured by Toshiba Machine Co., Ltd.) was prepared, and a mold having a mirror surface polished with # 6000 file was used, and the thickness was 100 mm. It was obtained by injection molding a flat plate molded article made of a polyester resin composition of × 100 mm × 2 mm. This flat molded product has a mirror surface transferred from a mold on one side. The cylinder temperature at the time of molding was 260 ° C., and the mold temperature was 60 ° C. Using a precision spectrophotometric colorimeter (trade name: “TC-1500SX”, manufactured by Tokyo Denshoku Co., Ltd.), Color on the mirror surface side of a flat plate molded product according to JIS Z 8722: 2009 and JIS Z 8781-4: 2013 The -b value was measured. Measurement conditions were a D65 light source, a 10 ° field of view, and a 0 ° -d method was used.

  (7) Fogging property (haze value): Using an injection molding machine (trade name: “EC100N”, manufactured by Toshiba Machine Co., Ltd.), a molded product made of a polyester resin composition was obtained. A plurality of small pieces having a size of about 30 mm × 30 mm were cut out from this molded product, and a total of 10 g was put in a glass tube (φ65 × 80 mm) having a bottom made of aluminum foil. This glass tube was set upright on a hot plate (trade name: “Neo Hot Plate HT-1000”, manufactured by AS ONE Corporation). Furthermore, after the glass tube was covered with a slide glass (78 mm × 76 mm × 1 mm), the set temperature of the hot plate was set to 160 ° C. and heat treatment was performed for 24 hours. As a result of the heat treatment, deposits due to decomposition products sublimated from the molded product were deposited on the inner wall of the slide glass. With respect to these slide glasses, haze values (haze degree%) were measured using a haze meter (trade name: “NDH2000”, manufactured by Nippon Denshoku Industries Co., Ltd.). It means that a polyester resin composition has low fogging property, so that a haze value is small (it is transparent).

  (8) Mold fouling acceleration test: An injection molding machine (trade name: “EC100N”, manufactured by Toshiba Machine Co., Ltd.) is prepared, and a continuous molding evaluation mold (outer diameter 30 mm, inner diameter 20 mm, thickness 3 mm) is used as a mold. And the flow end was a recess and no gas venting). Using this mold, the polyester resin composition is continuously molded by the short shot method so that components that promote mold contamination, such as outgas and oligomers, tend to accumulate in the recess on the opposite side of the gate portion. Was observed. The cylinder temperature at the time of molding was 260 ° C., the mold temperature was 50 ° 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 visually evaluated as follows using a grayscale-processed image in order to make the color of the image uniform.

A: No dirt is observed. B: Almost no dirt is observed. C: The dirt is blurry in the center near the recess on the opposite side of the gate. D: The center dirt near the recess on the opposite side of the gate is clear. Conspicuous black in outline.

(9) Thermal deformation temperature (load: 0.45 MPa)
Using an injection molding machine (trade name: “EC100N”, manufactured by Toshiba Machine Co., Ltd.), a multipurpose test piece of ISO-3167 was molded under the conditions of a cylinder temperature of 260 ° C. and a mold temperature of 60 ° C. With respect to this multi-purpose test piece, the heat distortion temperature when loaded at 0.45 MPa was measured according to ISO-75.

(10) Bleed-out property (visual inspection)
An injection molding machine (trade name: “EC100N”, manufactured by Toshiba Machine Co., Ltd.) is prepared, and a mold having a mirror surface polished with a # 14000 file is used and is made of a polyester resin composition of 100 mm × 100 mm × 2 mm. It was obtained by injection molding a flat plate molded product. This flat molded product has a mirror surface transferred from a mold on one side. The cylinder temperature at the time of molding was 260 ° C., the mold temperature was 60 ° C., and the cycle time was 40 seconds.
The molded product was put into a 160 ° C. gear oven, and after 24 hours, the presence or absence of bleed-out was confirmed visually in the sun outdoors (determined by comparison with the molded product before heat treatment). When bleed-out is confirmed, a rainbow pattern or the like is observed on the surface of the molded product.
A: No bleed out.
○: Bleed-out is confirmed only partly (sparsely).
X: Bleed out is observed on the entire surface of the molded product.

(11) Evaporation heat resistance test (diffuse reflectance)
An injection molding machine (trade name: “EC100N”, manufactured by Toshiba Machine Co., Ltd.) is prepared, and a mold having a mirror surface polished with a # 14000 file is used and is made of a polyester resin composition of 100 mm × 100 mm × 2 mm. It was obtained by injection molding a flat plate molded product. This flat molded product has a mirror surface transferred from a mold on one side. The cylinder temperature at the time of molding was 260 ° C., the mold temperature was 60 ° C., and the cycle time was 40 seconds.
Next, the molded product was placed in a vacuum deposition apparatus and brought into a reduced pressure state of about 1 × 10 ⁻⁵ Pa, and then the tungsten resistance heating element was energized and heated using aluminum as an evaporation source to evaporate the aluminum at a high temperature ( 2 minutes). The evaporated aluminum particles adhered to the surface of the molded product, and an aluminum vapor deposition film was formed on the entire surface of the molded product. The film thickness of the aluminum vapor deposition film was 80 nm.
The vapor-deposited molded product was put into a 160 ° C. gear oven, and after 24 hours, diffuse reflectance was measured using a reflection / transmittance meter HR-100 manufactured by Murakami Color Research Laboratory Co., Ltd. If the diffuse reflectance after heat treatment is 2% or less, it can be used practically without any problem. On the other hand, if it exceeds 2%, there is a possibility of practical problems due to deterioration of the appearance.

The compounding components used in Examples and Comparative Examples are shown below.
The polyester resin A is made of any of the following polybutylene terephthalate resins a, or made of any of the following polybutylene terephthalate resins a and a polyethylene terephthalate resin b.

One of the following was used as the polybutylene terephthalate resin a.
a-1: IV = 0.83 dl / g, terminal hydroxyl group = 95 eq / ton, acid value = 9 eq / ton, titanium atom content = 80 mg / kg (using a melt polymerization resin with IV = 0.78 dl / g, 210 Solid state polymerization was performed until IV = 0.83 dl / g was reached at 0 ° C.). However, 10 mg / kg of potassium acetate as a metal organic acid salt B is added at the time of melt polymerization of the above melt polymerization resin (after esterification reaction). A-2: IV = 0.83 dl / g, terminal hydroxyl group = 90 eq / ton, acid Valency = 6 eq / ton, titanium atom content = 80 mg / kg (using a melt polymerization resin with IV = 0.73 dl / g, solid state polymerization was performed at 210 ° C until IV = 0.83 dl / g was reached). However, 10 mg / kg of potassium acetate as the metal organic acid salt B is added at the time of melt polymerization of the above melt polymerization resin (after esterification reaction) a-3: IV = 0.83 dl / g (resin obtained by melt polymerization), Terminal hydroxyl group = 100 eq / ton, acid value = 10 eq / ton, titanium atom content = 80 mg / kg (no special treatment was performed to reduce the content of the linear oligomer). However, 10 mg / kg of potassium acetate as metal organic acid salt B is added at the time of melt polymerization of the above resin (after esterification reaction). A-4: IV = 0.83 dl / g (resin obtained by melt polymerization), terminal hydroxyl group = 100 eq / ton, acid value = 10 eq / ton, titanium atom content = 80 mg / kg (no special treatment was performed to reduce the content of the linear oligomer). However, 90 mg / kg of potassium acetate as a metal organic acid salt B was added at the time of melt polymerization of the resin (after esterification reaction). A-5: IV = 0.83 dl / g, terminal hydroxyl group = 95 eq / ton, acid value = 9 eq / ton, titanium atom content = 30 mg / kg (using a melt polymerization resin with IV = 0.78 dl / g, solid phase polymerization at 210 ° C. until reaching IV = 0.83 dl / g). However, metal organic acid salt B was not added. A-6: IV = 0.83 dl / g, terminal hydroxyl group = 95 eq / ton, acid value = 9 eq / ton, titanium atom content = 80 mg / kg (IV = 0.78 dl / g) g of melt polymerization resin was used and solid state polymerization was performed at 210 ° C. until IV = 0.83 dl / g was reached). However, metal organic acid salt B is added by master pellets during melt kneading a-7: IV = 0.83 dl / g, terminal hydroxyl group = 95 eq / ton, acid value = 9 eq / ton, titanium atom content = 30 mg / kg ( (A melt polymerization resin having IV = 0.78 dl / g was used, and solid-state polymerization was performed at 210 ° C. until IV = 0.83 dl / g was reached). However, metal organic acid salt B is added by master pellets during melt kneading a-8: IV = 0.83 dl / g, terminal hydroxyl group = 90 eq / ton, acid value = 6 eq / ton, titanium atom content = 80 mg / kg ( (A melt polymerization resin having IV = 0.73 dl / g was used, and solid-state polymerization was performed at 210 ° C. until IV = 0.83 dl / g was reached). However, metal organic acid salt B is added by master pellets during melt kneading a-9: IV = 0.83 dl / g, terminal hydroxyl group = 90 eq / ton, acid value = 6 eq / ton, titanium atom content = 30 mg / kg ( (A melt polymerization resin having IV = 0.73 dl / g was used, and solid-state polymerization was performed at 210 ° C. until IV = 0.83 dl / g was reached). However, metal organic acid salt B is added by master pellets during melt kneading a-10: IV = 0.83 dl / g (resin obtained by melt polymerization), terminal hydroxyl group = 100 eq / ton, acid value = 10 eq / ton, titanium Atomic content = 80 mg / kg (no special treatment to reduce the content of linear oligomers). However, metal organic acid salt B is added by master pellets during melt kneading a-11: IV = 0.83 dl / g (resin obtained by melt polymerization), terminal hydroxyl group = 100 eq / ton, acid value = 10 eq / ton, titanium Atomic content = 30 mg / kg (no special treatment to reduce the content of linear oligomers). However, metal organic acid salt B is added by master pellets during melt kneading.

  In addition, with respect to polybutylene terephthalate resin a-1 to a-4, the metal organic acid salt B which consists of potassium acetate or magnesium acetate of the above quantity was added at the time of superposition | polymerization. The remaining amount (content) of metal organic acid salt B in the polyester resin composition was as shown in Tables 1 to 5 below. For polybutylene terephthalate resins a-6 to a-11, a metal organic acid salt B made of potassium acetate or magnesium acetate is used using a master pellet prepared in advance at the time of melt kneading to obtain a polyester resin composition. It adjusted and added so that it might become content shown to the following Tables 1-5. The metal organic acid salt B was not added to the polybutylene terephthalate resin a-5.

  Polyethylene terephthalate resin b: IV = 0.62 dl / g, acid value = 30 eq / ton.

As the metal organic acid salt B, the following compounds were used.
B-1: Potassium acetate (Wako Pure Chemical Industries, Ltd.)
B-2: Magnesium acetate (manufactured by Wako Pure Chemical Industries, Ltd.)
B-3: Master pellet of potassium acetate (manufactured by Wako Pure Chemical Industries, Ltd.) B-4: Master pellet of magnesium acetate (manufactured by Wako Pure Chemical Industries, Ltd.).

  In addition, as the base resin of the master pellet, the same resin as the polybutylene terephthalate resin present in the polyester resin composition to be added was used. The content of the metal organic acid salt B in the master pellet is based on the content of potassium atoms for B-3, and the content of magnesium for B-4. As for the content, the potassium atom of B-3 is 0.2 mass part with respect to 100 mass parts of master pellets, and the magnesium atom of B-4 is 0.085 mass parts with respect to 100 mass parts of master pellets.

As the carboxylic acid reactive group-containing compound C, the following compounds were used.
C-1: Aliphatic polycarbodiimide compound (one with all isocyanate groups blocked at the end, trade name: “Carbodilite HMV-15CA”, manufactured by Nisshinbo Chemical Co., Ltd.)
C-2: Aliphatic polycarbodiimide compound (having an isocyanate group at the terminal, trade name: “Carbodilite LA-1”, manufactured by Nisshinbo Chemical Co., Ltd.).

As the styrene resin D, the following compounds were used.
D-1: acrylonitrile - styrene copolymer (suspension product) [(trade name: "AP-20", UMG-ABS Ltd. ^(MVR = 38cm 3 / 10min; measurement conditions 220 ℃, 10kgf), Mw = 130,000, styrene component content 70 to 75% by mass]
D-2: acrylonitrile - styrene copolymer (suspension product) [trade name: "AP-50", UMG-ABS Ltd. ^(MVR = 8.5cm 3 / 10min; measurement conditions 220 ° C., 10 kgf), Mw = 220,000, styrene component content 70-75% by mass]
Mw was measured by gel permeation chromatography under the following conditions.

Gel permeation chromatography analyzer: Product name: “HLC-8220”, manufactured by Tosoh Corporation Column: 2 TSKgel SuperHZM-H, 1 TSKgel SuperHZ2000 (TOSOH) Guard column: TSKgel guardcolumn SuperHZ-H
Eluent: Tetrahydrofuran Flow rate: 0.35 ml / min
Sample dissolution solvent: tetrahydrofuran Sample dissolution concentration: 0.05% by mass
Injection volume: 10 μl
Detector: Differential refractometer (RI)
Temperature: 40 ° C
Standard sample: Standard sample Polystyrene Standards (manufactured by Tosoh Corporation).

  Polycarbonate resin [trade name: “LEXAN141”, manufactured by SABIC (MFR = 10.5 g / 10 min; 300 ° C., 1.2 kgf)]

As the release agent E, the following compounds were used.
E-1: Triglycerin behenic acid full ester (trade name: “Poem TR-FB”, manufactured by Riken Vitamin Co., Ltd.)
E-2: A mixture of pentaerythritol stearic acid full ester and pentaerythritol palmitic acid full ester (trade name: “Ricester EW-440A”, manufactured by Riken Vitamin Co., Ltd.).

  As a stabilizer, an antioxidant (trade name: “IRGANOX1010”, manufactured by BASF) was used. This stabilizer was contained in an amount of 0.2 parts by mass with respect to 100 parts by mass of the polyester resin A.

(Examples 1-17, Comparative Examples 1-17)
The blended components blended in the combinations shown in Tables 1 to 5 were kneaded with a same-direction twin-screw extruder set at a cylinder temperature of 250 ° C. (Example 14 and Comparative Example 10 was 260 ° C.), and the resulting strand was water-cooled. And pelletized. Each obtained pellet was dried at 130 ° C. for 4 hours to obtain a polyester resin composition corresponding to each example and each comparative example. The above-described evaluation tests (4) to (11) were performed on these polyester resin compositions.

  Regarding the amount of the metal organic acid salt B, in the Examples and Comparative Examples in which the metal organic acid salt B was added during polymerization, the residual amount (content) in the polyester resin composition after melt-kneading relative to the amount at the time of addition. (The possibility of distilling off during the depressurization process in the late stage of polymerization and the vent deaeration process during melt kneading is considered). In Comparative Examples 3 and 4 (examples using polybutylene terephthalate resin a-5), metal organic acid salt B was not added. The above results are shown in Tables 1 to 5 below.

  As shown in Tables 1 to 3, the polyester resin compositions of Examples 1 to 17 have very little mold contamination during continuous molding, and the haze value of the glass plate after the fogging test is 5% or less. It can be seen that it has excellent properties. Furthermore, the bleed-out property is also good (no bleed-out is seen) and the appearance after heat treatment is also excellent. When the compositions were the same as in Example 3 and Example 5, the lower the titanium atom content, the lower the haze value, and the fogging property tended to be better.

  As shown in Tables 4 and 5, Comparative Examples 1 to 17 are examples in which the linear oligomer content is larger than the specified range, examples that do not include the metal organic acid salt B, and examples that the metal organic acid salt B is excessive. , An example not containing the carboxylic acid reactive group-containing compound C, an example in which the carboxylic acid reactive group containing compound C is excessive, or an example in which the content ratio of the polyethylene terephthalate resin b in the polyester resin A is greater than the specified range This corresponds to at least one of the examples not containing the resin D, and the mold is more easily soiled than the examples, and the haze value tends to be high and the fogging property tends to be poor and the bleed-out property tends to be poor. . Comparing the case where the composition other than the carboxylic acid reactive group-containing compound C is the same as in Example 3 and Comparative Example 8, the amount of linear oligomer is reduced by containing the carboxylic acid reactive group-containing compound C. There was a tendency to.

In Comparative Example 2, since the amount of the metal organic acid salt B added during the polymerization was large, the decomposition reaction was accelerated during the polymerization, the content of the linear oligomer increased, and both the Color-b value and the haze value were deteriorated. . In Comparative Example 10, the content ratio of the polyethylene terephthalate resin b was large, and the mold contamination and the haze value were deteriorated as compared with Examples 1 to 17.
Comparative Examples 13 to 15 did not contain the styrene resin D, and the bleed-out property was deteriorated. In Comparative Example 16, the styrene resin D was excessively contained, the compatibility with the polyester resin was deteriorated, and the surface of the flat plate was roughened and whitened. Therefore, the Color-b value and the diffuse reflectance could not be measured. Comparative Example 17 contained polycarbonate as an amorphous resin, and the surface of the flat plate was whitened after heat treatment, and the diffuse reflectance was remarkably increased.
Further, when the heat deformation temperatures of Examples 13 and 14 and Comparative Example 10 having different content ratios of polyethylene terephthalate resin b are compared, Example 13 is 145 ° C. and Example 14 is 121 ° C., while Comparative Example 10 is 75 Since it became ° C., Comparative Example 10 was evaluated as having extremely low heat resistance.

  Although the embodiments and examples of the present invention have been described as described above, it is also planned from the beginning to appropriately combine the configurations of the above-described embodiments and examples.

  It should be understood that the embodiments and examples disclosed herein are illustrative and non-restrictive in every respect. The scope of the present invention is defined by the terms of the claims, rather than the description above, and is intended to include any modifications within the scope and meaning of the claims.

Claims (9)

A polyester resin composition comprising a polyester resin A containing 70 to 100% by mass of polybutylene terephthalate resin and 0 to 30% by mass of polyethylene terephthalate resin,
The polyester resin composition has a metal organic acid salt B that is one or both of an organic acid salt of an alkali metal and an organic acid salt of an alkaline earth metal, and 0.05 to 3 parts by weight of carboxylic acid reactive group-containing compound C and 0.5 to 10 parts by weight of styrene resin D,
The polyester resin composition contains one or both of an alkali metal atom and an alkaline earth metal atom in an amount of 0.000005 to 0.05 parts by mass with respect to 100 parts by mass of the polyester resin A, and
The polyester resin composition is a polyester resin composition in which the content of the linear oligomer of polybutylene terephthalate, or the content of the linear oligomer of polybutylene terephthalate and the linear oligomer of polyethylene terephthalate is 1000 mg / kg or less.   The polyester resin composition includes 0.0005 to 0.05 parts by mass of one or both of the alkali metal atoms and the alkaline earth metal atoms with respect to 100 parts by mass of the polyester resin A. The polyester resin composition as described.   The polyester resin composition according to claim 1, wherein the polyester resin composition has a titanium atom content of 50 mg / kg or less.   The polyester resin composition according to claim 1, wherein the styrene resin D is a styrene-acrylonitrile copolymer.   The polyester resin composition according to claim 1, wherein the carboxylic acid reactive group-containing compound C is a polycarbodiimide compound.   The polyester resin composition according to any one of claims 1 to 5, wherein the metal species of the metal organic acid salt B is one or more selected from the group consisting of lithium, sodium, potassium, calcium, and magnesium. .   The metal organic acid salt B is one or more selected from the group consisting of lithium acetate, sodium acetate, potassium acetate, calcium acetate, magnesium acetate, lithium benzoate, sodium benzoate and potassium benzoate, Item 7. The polyester resin composition according to any one of Items 1 to 6.   The component for light reflectors containing the polyester resin composition in any one of Claims 1-7.   A light reflector, wherein a light reflecting metal layer is formed on at least a part of the surface of the light reflector component according to claim 8.