JP6044058B2 - Polycarbonate resin composition and molded product - Google Patents

Description

  The present invention relates to a polycarbonate resin composition excellent in weather resistance, hue, heat resistance, thermal stability, mechanical strength, and the like, and a molded product thereof.

Polycarbonate resins are generally composed of bisphenols as monomer components, taking advantage of transparency, heat resistance, mechanical strength, etc., and electrical / electronic parts, automotive parts, medical parts, building materials, films, sheets, bottles It is widely used as so-called engineering plastics in the fields of optical recording media and lenses.
However, conventional polycarbonate resins are limited in use outdoors or in the vicinity of lighting devices, because their hue, transparency, and mechanical strength deteriorate when used in places exposed to ultraviolet rays or visible light for a long time. .

In order to solve such problems, a method of adding a benzophenone ultraviolet absorber, a benzotriazole ultraviolet absorber, or a benzoxazine ultraviolet absorber to a polycarbonate resin is widely known (for example, Non-Patent Document 1).
However, when such an ultraviolet absorber is added, although the hue after UV irradiation is improved, the hue, heat resistance, and transparency of the resin are deteriorated in the first place. There were problems such as contamination of the mold.

  Since the bisphenol compound used in the conventional polycarbonate resin has a benzene ring structure, it absorbs a large amount of ultraviolet rays. This causes a deterioration in the weather resistance of the polycarbonate resin. Therefore, an aliphatic dihydroxy compound having no benzene ring structure in the molecular skeleton. If a cyclic dihydroxy compound monomer unit having an ether bond in the molecule, such as a compound, an alicyclic dihydroxy compound, or isosorbide, is used, it is expected that the weather resistance is improved in principle. Among them, a polycarbonate resin using isosorbide obtained from biomass resources as a monomer is excellent in heat resistance and mechanical strength, so that many studies have been made in recent years (for example, Patent Documents 1 to 6). .

  However, cyclic dihydroxy compounds having an ether bond in the molecule, such as the above aliphatic dihydroxy compounds, alicyclic dihydroxy compounds, and isosorbide, do not have phenolic hydroxyl groups, and thus are widely known as methods for producing polycarbonate resins using bisphenol A as a raw material. It is difficult to polymerize by the conventional interface method, and it is usually produced by a method called a transesterification method or a melting method. In this method, the dihydroxy compound and a carbonic acid diester such as diphenyl carbonate are transesterified at a high temperature of 200 ° C. or higher in the presence of a basic catalyst, and the polymerization proceeds by removing by-product phenol and the like out of the system, A polycarbonate resin is obtained. However, a polycarbonate resin obtained using a monomer having no phenolic hydroxyl group as described above is inferior in thermal stability to a polycarbonate resin obtained using a monomer having a phenolic hydroxyl group such as bisphenol A. In addition, there is a problem in that coloring occurs during polymerization and molding that are exposed to high temperatures, and as a result, ultraviolet rays and visible light are absorbed to deteriorate weather resistance. In particular, when a monomer having an ether bond in the molecule, such as isosorbide, is used, the hue is remarkably deteriorated, and it is difficult to solve the improvement in brightness. Furthermore, when it is used as various molded products, it is melt-molded at a high temperature. At that time, a material having good thermal stability and excellent moldability and mold release properties has been demanded.

In addition, a method using a filler for improving the rigidity, dimensional stability, heat distortion temperature and the like of the polycarbonate resin is known. However, generally, when the hue of the polycarbonate resin before mixing the filler is poor, there is a problem that the hue after mixing the filler is further deteriorated.

International Publication No. 04/111106 Pamphlet Japanese Patent Laid-Open No. 2006-232897 JP 2006-28441 A JP 2008-24919 A JP 2009-91404 A JP 2009-91417 A

Polycarbonate resin handbook (issued by Seiichi Honma, published by Nikkan Kogyo Shimbun, August 28, 1992)

Furthermore, the present inventors have found that there is a problem that it is necessary to improve the weather resistance of a polycarbonate resin composition containing an ultraviolet absorber.
An object of the present invention is to provide a polycarbonate resin composition excellent in weather resistance, hue, heat resistance, thermal stability, and mechanical strength, and a molded product thereof, by solving the above-mentioned conventional problems.

  As a result of intensive studies to solve the above problems, the present inventor has obtained a specific amount of a polycarbonate resin containing at least a structural unit derived from a dihydroxy compound having a site represented by the following formula (1) in the molecule. A polycarbonate resin composition comprising an ultraviolet absorber, and a polycarbonate resin composition containing a specific amount of a specific metal as a catalyst for the polycarbonate resin has not only excellent weather resistance but also excellent weather resistance, It has been found that it has hue, heat resistance, thermal stability, mechanical strength, etc., and has reached the present invention.

That is, the gist of the present invention resides in the following [1] to [9].
[1] A polycarbonate resin composition comprising a polycarbonate resin containing at least a structural unit derived from a dihydroxy compound having a site represented by the following formula (1) in a part of the structure, and an ultraviolet absorber, the polycarbonate resin At least one metal selected from the group consisting of lithium and a metal of Group 2 of the long-period periodic table, containing 0.05 part by weight or more and 5 parts by weight or less of an ultraviolet absorber with respect to 100 parts by weight of the resin The polycarbonate resin composition is characterized in that the amount of the metal contained as a catalyst is 20 ppm by weight or less in total with respect to the entire polycarbonate resin composition.

(However, the site represented by the above formula (1) unless a portion constituting a _-CH 2 -O-H.)

[2] The polycarbonate resin composition according to [1], wherein the dihydroxy compound having a part represented by the formula (1) in a part of the structure is a dihydroxy compound represented by the following formula (2).

[3] The polycarbonate resin composition according to [1] or [2], wherein the polycarbonate resin includes a structural unit derived from an aliphatic dihydroxy compound.

[4] The polycarbonate resin is obtained by polycondensation of a dihydroxy compound containing a dihydroxy compound having a site represented by the formula (1) in a part of the structure with a carbonic acid diester represented by the following formula (3). The polycarbonate resin composition according to any one of [1] to [3].

(In the above formula (2), A ¹ and A ² are each independently a substituted or unsubstituted aliphatic hydrocarbon group having 1 to 18 carbon atoms, or a substituted or unsubstituted aromatic hydrocarbon group. And A ¹ and A ² may be the same or different.)

[5] The polycondensation is performed in the presence of a catalyst, and the catalyst is at least one metal compound selected from the group consisting of a lithium compound and a metal of Group 2 of the long-period periodic table, And the polycarbonate resin composition as described in [4] whose total amount of these metal compounds is 20 micromol or less as a metal amount with respect to 1 mol of dihydroxy compounds used.

[6] The polycarbonate resin composition according to [5], wherein the catalyst is at least one metal compound selected from the group consisting of a magnesium compound and a calcium compound.
[7] The polycarbonate resin composition according to any one of [1] to [6], wherein a total content of lithium, sodium, potassium and cesium in the polycarbonate resin is 1 ppm by weight or less as a metal amount. object.

[8] A polycarbonate resin molded product obtained by molding the polycarbonate resin composition according to any one of [1] to [7].

[9] The polycarbonate resin molded product according to [8], which is molded by an injection molding method.

  According to the present invention, not only has excellent weather resistance, but also excellent hue, heat resistance, thermal stability, and mechanical strength, electric and electronic parts, injection molding fields such as automotive parts, film, A polycarbonate resin composition applicable to a wide range of fields such as the sheet field, bottle, and container field can be provided, and a polycarbonate resin composition suitable for applications exposed to light including ultraviolet rays such as outdoors and lighting parts is provided. It becomes possible to do. It should be noted that in the present invention, it is not essential to exhibit all the effects, as long as it exhibits at least one excellent effect among weather resistance, hue, heat resistance, thermal stability, and mechanical strength. The effects of the present invention are exhibited.

  DESCRIPTION OF EMBODIMENTS Embodiments of the present invention will be described in detail below. However, the description of the constituent elements described below is an example (representative example) of an embodiment of the present invention. It is not limited to the contents. In addition, when it describes with "-" in this specification, it shall use as an expression including the numerical value or physical quantity before and behind that.

1. Polycarbonate resin composition
The polycarbonate resin composition of the present invention comprises a polycarbonate resin containing at least a structural unit derived from a dihydroxy compound having a site represented by the following formula (1) in a part of the structure, and an ultraviolet absorber. Wherein the ultraviolet light absorber is contained in an amount of 0.05 part by weight or more and 5 parts by weight or less with respect to 100 parts by weight of the polycarbonate resin, and selected from the group consisting of lithium and a metal of Group 2 of the long-period periodic table. The amount of the metal contained as the catalyst of the polycarbonate resin is 20 ppm by weight or less in total with respect to the whole polycarbonate resin composition. .

(However, the site represented by the above formula (1) unless a portion constituting a _-CH 2 -O-H.)

  The details of the polycarbonate resin, the ultraviolet absorber and the blending amount thereof in the polycarbonate resin composition of the present invention will be described later. The polycarbonate resin composition of the present invention is a group consisting of lithium and a metal of Group 2 of the long-period periodic table. The at least one metal selected from the above may be referred to as a polycarbonate resin containing at least a structural unit derived from a dihydroxy compound having a site represented by the above formula (1) (hereinafter referred to as “polycarbonate resin used in the present invention”). ) And a metal contained as the catalyst, that is, lithium and a metal of Group 2 of the long-period type periodic table in a total of 20 ppm by weight or less based on the entire polycarbonate resin composition. The total content of lithium and long-period group 2 metal in the polycarbonate resin composition is preferably small in order to make the polycarbonate resin composition excellent in light resistance, more preferably It is 10 weight ppm or less, More preferably, it is 5 weight ppm or less.

However, in the polycarbonate resin composition of the present invention, lithium and the metal of Group 2 of the long-period periodic table are derived from the catalyst used for the production of the polycarbonate resin and are contained in the polycarbonate resin composition, Since it is difficult to completely remove the contained metals out of the system industrially, the total content is usually 0.01 ppm by weight or more, preferably 0. 05 ppm by weight or more,
More preferably, it is 0.1 weight ppm or more.

  The long-period periodic table group 2 metal contained in the polycarbonate resin composition of the present invention is beryllium, magnesium, calcium, strontium, barium, and among these long-period periodic table group 2 metals, The polycarbonate resin composition preferably contains magnesium or calcium, and more preferably contains calcium.

  Further, the polycarbonate resin composition of the present invention includes a metal selected from sodium, potassium and cesium, but the total content of sodium, potassium and cesium in the polycarbonate resin composition is based on the total polycarbonate resin composition. The amount of metal is preferably 1 ppm by weight or less. Sodium, potassium and cesium may be mixed not only from the catalyst used in the production of the raw material polycarbonate resin, but also from raw materials and reaction equipment such as dihydroxy compounds. Therefore, even when the polycarbonate resin composition is produced, these totals The amount is more preferably 0.8 ppm by weight or less, and still more preferably 0.7 ppm by weight or less as the amount of metal. When the total content of metals selected from sodium, potassium, and cesium is within the above range, the polycarbonate resin composition has excellent weather resistance.

  The amount of metal in the polycarbonate resin composition can be measured by various conventionally known methods. After recovering the metal in the polycarbonate resin by a method such as wet ashing, atomic emission, atomic absorption, Inductively Coupled Plasma ( ICP) and other methods can be used.

The polycarbonate resin composition of the present invention has an initial yellow index (YI) value based on ASTM D 1925-70 measured by reflected light as a molded body (thickness 3 mm) from the viewpoint of weather resistance, and YI ₁ , In an environment of 63 ° C. and relative humidity of 50%, the yellow index (YI) value after irradiation for 100 hours at an irradiance of 1.5 kW / m ² with a wavelength of 300 nm to 400 nm using a metal halide lamp is defined as YI ₂ In this case, it is preferable that | YI ₁ −YI ₂ | ≦ 6.0 or less, more preferably 5.0 or less, and still more preferably 4.0 or less. In addition, the irradiation process using the metal halide lamp in this invention means the metal halide lamp irradiation test in the Example mentioned later.

  In order to reduce the difference in the absolute value of the YI value before and after the irradiation with the metal hydride lamp, that is, to make the polycarbonate resin composition have excellent light resistance, it is used, for example, when producing the polycarbonate resin used in the present invention. Select the type and amount of the catalyst as appropriate, select the temperature and time during the polycondensation of the polycarbonate resin as appropriate, compounds having an ultraviolet absorbing ability in the polycarbonate resin, such as reducing residual phenol, residual diphenyl carbonate, dihydroxy compounds, etc. It can be produced by reducing the amount of a substance having absorption in the ultraviolet region as a raw material monomer, or reducing the amount of a substance having absorption in the ultraviolet region contained as an impurity in the raw material. In particular, the type and amount of the catalyst, the temperature and time during the polycondensation are important, and in particular, the conditions that are preferred in the description of the polycarbonate resin described below are adopted, and as described above, the lithium in the entire polycarbonate resin composition And it is preferable to contain a long period type periodic table group 2 metal in a specific amount or less.

  From the viewpoint of weather resistance, the polycarbonate resin composition of the present invention is formed as a molded body (thickness 3 mm), and the metal measures the haze value before and after the ride lamp irradiation by the method described in the examples below. The difference obtained by subtracting the haze value before irradiation from the haze value after irradiation is preferably 18 or less, more preferably 15 or less, and even more preferably 11 or less.

  The polycarbonate resin composition of the present invention preferably contains 60 ppm by weight or less of carbonic acid diester represented by the following formula (3) from the viewpoint of hue. Since the carbonic acid diester represented by the following formula (3) is mainly derived from the raw material of the polycarbonate resin, the details will be described in the description of the polycarbonate resin.

(In the above formula (3), A ¹ and A ² are each independently a substituted or unsubstituted aliphatic hydrocarbon group having 1 to 18 carbon atoms, or a substituted or unsubstituted aromatic hydrocarbon group. And A ¹ and A ² may be the same or different.)

  In addition, the polycarbonate resin composition of the present invention preferably has an aromatic monohydroxy compound content of 700 ppm by weight or less, and 500 ppm by weight with respect to the entire polycarbonate resin composition from the viewpoint of light resistance and odor reduction. More preferably, it is more preferably 300 ppm by weight or less. The aromatic monohydroxy compound is derived from what is mainly contained in the raw material polycarbonate resin and is contained in the polycarbonate resin composition. The aromatic monohydroxy compound is described in detail in the description of the polycarbonate resin below. Describe. However, the aromatic monohydroxy compound contained in the polycarbonate resin composition is used in the meaning excluding those that may be contained in the polycarbonate resin composition as an “antioxidant”.

2. Polycarbonate Resin A method for producing a polycarbonate resin (hereinafter sometimes referred to as “polycarbonate resin used in the present invention”) blended in the polycarbonate resin composition of the present invention will be described in detail below.

<Raw material>
(Dihydroxy compound)
The polycarbonate resin used in the present invention is a structural unit derived from a dihydroxy compound having a site represented by the following formula (1) in a part of the structure (hereinafter sometimes referred to as “dihydroxy compound used in the present invention”). At least. That is, the dihydroxy compound used in the present invention refers to a compound containing at least two hydroxyl groups and a site represented by the following formula (1).

(However, the site represented by the above formula (1) unless a portion constituting a _-CH 2 -O-H.)

The dihydroxy compound used in the present invention is not particularly limited as long as it is a dihydroxy compound having a site represented by the above formula (1) in a part of the structure, but specifically, diethylene glycol, triethylene glycol Oxyalkylene glycols such as tetraethylene glycol, 9,9-bis (4- (2-hydroxyethoxy) phenyl) fluorene, 9,9-bis (4- (2-hydroxyethoxy) -3-methylphenyl) fluorene 9,9-bis (4- (2-hydroxyethoxy) -3-isopropylphenyl) fluorene, 9,9-bis (4- (2-hydroxyethoxy) -3-isobutylphenyl) fluorene, 9,9-bis (4- (2-hydroxyethoxy) -3-tert-butylphenyl) fluorene, 9,9 Bis (4- (2-hydroxyethoxy) -3-cyclohexylphenyl) fluorene, 9,9-bis (4- (2-hydroxyethoxy) -3-phenylphenyl) fluorene, 9,9-bis (4- (2 -Hydroxyethoxy) -3,5-dimethylphenyl) fluorene, 9,9-bis (4- (2-hydroxyethoxy) -3-tert-butyl-6-methylphenyl) fluorene, 9,9-bis (4- (3-hydroxy-2,2-dimethylpropoxy) phenyl) fluorene and the like, a compound having an aromatic group in the side chain and an ether group bonded to the aromatic group in the main chain, represented by the following formula (2) And compounds having a cyclic ether structure such as a dihydroxy compound represented by the following formula (4) and a dihydroxy compound represented by the following formula (5). Among them, diethylene glycol and triethylene glycol are preferable from the viewpoint of easy availability, handling, reactivity during polymerization, and hue of the obtained polycarbonate resin, and compounds having a cyclic ether structure from the viewpoint of heat resistance. In view of the physical stability of the structure, a dihydroxy compound having two cyclic ether structures such as a dihydroxy compound represented by the following formula (2) and a dihydroxy compound represented by the following formula (4) is more preferable. Anhydrosugar alcohols represented by dihydroxy compounds represented by the following formula (2) are particularly preferred.

  These dihydroxy compounds may be used alone or in combination of two or more depending on the required performance of the obtained polycarbonate resin.

  Examples of the dihydroxy compound represented by the above formula (2) include isosorbide, isomannide and isoidet which are in a stereoisomeric relationship, and these may be used alone or in combination of two or more. May be.

  Of these dihydroxy compounds, it is preferable to use a dihydroxy compound having no aromatic ring structure from the viewpoint of the light resistance of the polycarbonate resin, and among them, it is abundant as a plant-derived resource and is produced from various easily available starches. Isosorbide obtained by dehydrating and condensing sorbitol is most preferable from the viewpoints of availability and production, light resistance, optical properties, moldability, heat resistance, and carbon neutral.

  The polycarbonate resin used in the present invention may contain a structural unit derived from a dihydroxy compound other than the dihydroxy compound used in the present invention (hereinafter sometimes referred to as “other dihydroxy compound”), and other dihydroxy compounds. Examples thereof include aliphatic dihydroxy compounds such as chain aliphatic dihydroxy compounds and alicyclic dihydroxy compounds, and aromatic bisphenols. Among these, aliphatic dihydroxy compounds are preferable, and alicyclic dihydroxy compounds are more preferable.

The chain aliphatic dihydroxy compound is a compound having a hydrocarbon skeleton having a chain structure and two hydroxyl groups, and does not include a compound having an oxygen atom such as an ether group except for the hydroxyl group. The chain aliphatic dihydroxy compound includes a straight chain aliphatic dihydroxy compound and a branched chain aliphatic dihydroxy compound. Examples of the linear aliphatic dihydroxy compound include ethylene glycol, 1,3-propanediol, 1,2-propanediol, 1,4-butanediol, 1,3-butanediol, 1,2-butanediol, 1,5 -Pentanediol, 1,6-hexanediol, 1,7-heptanediol, 1,5-heptanediol, 1,10-decanediol, 1,12-dodecanediol and the like. Examples of the branched aliphatic dihydroxy compound include neopentyl glycol and hexylene glycol.

  The alicyclic dihydroxy compound is a compound having a hydrocarbon skeleton having a cyclic structure and two hydroxyl groups, and the hydroxyl group may be directly bonded to the cyclic structure or via a substituent such as an alkylene group. And may be bonded to a ring structure. The cyclic structure may be monocyclic or polycyclic. As a suitable thing of an alicyclic dihydroxy compound, the alicyclic dihydroxy compound which has the 5-membered ring structure mentioned below, and the alicyclic dihydroxy compound which has a 6-membered ring structure are mentioned. Since the rigidity of the polycarbonate resin obtained by using the alicyclic dihydroxy compound which has a 5-membered ring structure and the alicyclic dihydroxy compound which has a 6-membered ring structure can be improved as an alicyclic dihydroxy compound, it is preferable. The carbon number of the alicyclic dihydroxy compound is usually 70 or less, preferably 50 or less, more preferably 30 or less. The greater the number of carbons, the higher the heat resistance of the resulting polycarbonate resin. However, the smaller the number of carbons, the easier the purification and the easy procurement of raw materials.

  Examples of alicyclic dihydroxy compounds having a five-membered ring structure include tricyclodecanediols, pentacyclopentadecanediols, cyclopentanediols such as 1,3-cyclopentanediol, and 1,3-cyclopentanedimethanol. Cyclopentanedimethanols, 2,6-decalindiol, 1,5-decalindiol, decalindiols such as 2,3-decalindiol, 1,5-decalindimethanol, 2,6-decalindimethanol, 2, Examples include decalin dimethanols such as 3-decalin dimethanol, tricyclodecane diols, tricyclodecane dimethanols, and pentacyclopentadecane dimethanols.

  Examples of alicyclic dihydroxy compounds having a 6-membered ring structure include cyclohexanediols such as 1,2-cyclohexanediol, 1,3-cyclohexanediol, 1,4-cyclohexanediol, and 2-methyl-1,4-cyclohexanediol. , Cyclohexene diols such as 4-cyclohexene-1,2-diol, norbornane diols such as 2,3-norbornane diol, 2,5-norbornane diol, 1,3-adamantane diol, 2,2-adamantane diol, etc. Adamantanediols, 1,2-cyclohexanedimethanol, 1,3-cyclohexanedimethanol, cyclohexanedimethanols such as 1,4-cyclohexanedimethanol, cyclohexenediols such as 4-cyclohexene-1,2diol, - norbornane methanol, 2,5-norbornane methanol, etc. norbornanedimethanol such, 1,3-adamantane dimethanol, etc. adamantane dimethanol such as 2,2-adamantane dimethanol and the like.

Aromatic bisphenols include 2,2-bis (4-hydroxyphenyl) propane [= bisphenol A], 2,2-bis (4-hydroxy-3,5-dimethylphenyl) propane, 2,2-bis ( 4-hydroxy-3,5-diethylphenyl) propane, 2,2-bis (4-hydroxy- (3,5-diphenyl) phenyl) propane, 2,2-bis (4-hydroxy-3,5-dibromophenyl) ) Propane, 2,2-bis (4-hydroxyphenyl) pentane, 2,4'-dihydroxy-diphenylmethane, bis (4-hydroxyphenyl) methane, bis (4-hydroxy-5-nitrophenyl) methane, 1,1 -Bis (4-hydroxyphenyl) ethane, 3,3-bis (4-hydroxyphenyl) pentane, 1,1-bis (4-hydro) Xylphenyl) cyclohexane, bis (4-hydroxyphenyl) sulfone, 2,4′-dihydroxydiphenylsulfone, bis (4-hydroxyphenyl) sulfide, 4,4′-dihydroxydiphenyl ether, 4,4′-dihydroxy-3,3 ′ -Dichlorodiphenyl ether, 9,9-bis (4- (2-hydroxyethoxy-2-methyl) phenyl) fluorene, 9,9-bis (4-hydroxyphenyl) fluorene, 9,9-bis (4-hydroxy-2) -Methylphenyl) fluorene and the like.

  Among the other dihydroxy compounds listed above, from the viewpoint of light resistance of the polycarbonate resin, dihydroxy compounds having no aromatic ring structure in the molecular structure, that is, dihydroxy compounds such as chain aliphatic dihydroxy compounds and alicyclic dihydroxy compounds. It is preferable to use a compound, and it is more preferable to use an alicyclic dihydroxy compound. As the chain aliphatic dihydroxy compound, 1,3-propanediol, 1,4-butanediol, and 1,6-hexanediol are particularly preferable. As the alicyclic dihydroxy compound, 1,4-cyclohexanedimethanol, Tricyclodecane dimethanol is preferred.

  By using these other dihydroxy compounds, it is possible to obtain effects such as improvement in flexibility of polycarbonate resin, improvement in heat resistance, improvement in moldability, but structural units derived from other dihydroxy compounds. If the content ratio is too large, mechanical properties and heat resistance may be lowered. Therefore, the ratio of the structural unit derived from the dihydroxy compound used in the present invention to the structural unit derived from all dihydroxy compounds is 20 It is preferably at least mol%, more preferably at least 30 mol%, particularly preferably at least 50 mol%.

  The dihydroxy compound used in the present invention may contain a stabilizer such as a reducing agent, antioxidant, oxygen scavenger, light stabilizer, antacid, pH stabilizer, heat stabilizer, etc. Since the dihydroxy compound used in the invention is easily altered, it is preferable to include a basic stabilizer. Basic stabilizers include Group 1 or Group 2 metal hydroxides, carbonates, phosphates, phosphites, hypophosphites in the Long Periodic Periodic Table (Nomenclature of Inorganic Chemistry IUPAC Recommendations 2005). Salts, borates, fatty acid salts, tetramethylammonium hydroxide, tetraethylammonium hydroxide, tetrapropylammonium hydroxide, tetrabutylammonium hydroxide, trimethylethylammonium hydroxide, trimethylbenzylammonium hydroxide, trimethylphenylammonium hydroxide, Triethylmethylammonium hydroxide, triethylbenzylammonium hydroxide, triethylphenylammonium hydroxide, tributylbenzylammonium hydroxide, tributylphenylan Basic ammonium compounds such as nium hydroxide, tetraphenylammonium hydroxide, benzyltriphenylammonium hydroxide, methyltriphenylammonium hydroxide, butyltriphenylammonium hydroxide, 4-aminopyridine, 2-aminopyridine, N, N -Dimethyl-4-aminopyridine, 4-diethylaminopyridine, 2-hydroxypyridine, 2-methoxypyridine, 4-methoxypyridine, 2-dimethylaminoimidazole, 2-methoxyimidazole, imidazole, 2-mercaptoimidazole, 2-methylimidazole And amine compounds such as aminoquinoline. Of these, sodium or potassium phosphates and phosphites are preferred, and disodium hydrogen phosphate and disodium hydrogen phosphite are particularly preferred because of their effects and ease of distillation removal described below.

  The content of these basic stabilizers in the dihydroxy compound used in the present invention is not particularly limited, but if it is too small, the effect of preventing the alteration of the dihydroxy compound used in the present invention may not be obtained, and it is too much. And may cause modification of the dihydroxy compound used in the present invention, and is usually 0.0001% by weight to 1% by weight, preferably 0.001% by weight to 0.1% by weight based on the dihydroxy compound used in the present invention. %.

Further, when the dihydroxy compound used in the present invention containing these basic stabilizers is used as a raw material for producing polycarbonate resin, the basic stabilizer itself becomes a polymerization catalyst, and it becomes difficult to control the polymerization rate and quality. In order to deteriorate the initial hue and consequently deteriorate the light resistance of the molded product, it is preferable to remove the basic stabilizer by ion exchange resin or distillation before using it as a raw material for producing the polycarbonate resin.

  When the dihydroxy compound used in the present invention has a cyclic ether structure such as isosorbide, it is easily oxidized by oxygen. Therefore, during storage and production, in order to prevent decomposition by oxygen, water should not be mixed, It is important to use an oxygen scavenger or handle under a nitrogen atmosphere. When isosorbide is oxidized, decomposition products such as formic acid may be generated. For example, when isosorbide containing these decomposition products is used as a polycarbonate resin production raw material, there is a possibility that the resulting polycarbonate resin may be colored, and the physical properties may be significantly deteriorated. The polymer having a high molecular weight may not be obtained.

  In order to obtain the dihydroxy compound used in the present invention which does not contain the above oxidative decomposition product, and in order to remove the aforementioned basic stabilizer, it is preferable to carry out distillation purification. The distillation in this case may be simple distillation or continuous distillation, and is not particularly limited. As distillation conditions, it is preferable to carry out distillation under reduced pressure in an inert gas atmosphere such as argon or nitrogen. In order to suppress thermal denaturation, it is 250 ° C. or lower, preferably 200 ° C. or lower, particularly 180 °. It is preferable to carry out under the conditions of ℃ or less.

  By such purification by distillation, the formic acid content in the dihydroxy compound used in the present invention is preferably 20 ppm by weight or less, more preferably 10 ppm by weight or less, and particularly preferably 5 ppm by weight or less. When a dihydroxy compound containing a dihydroxy compound to be used is used as a raw material for producing a polycarbonate resin, it is possible to produce a polycarbonate resin excellent in hue and thermal stability without impairing polycondensation reactivity. The formic acid content is measured by ion chromatography.

(Carbonated diester)
The polycarbonate resin used in the present invention can be obtained by polycondensation by a transesterification reaction using the dihydroxy compound containing the dihydroxy compound used in the present invention and the carbonic acid diester as raw materials. As a carbonic acid diester used, what is normally represented by following formula (3) is mentioned. These carbonic acid diesters may be used alone or in combination of two or more.

(In the above formula (3), A ¹ and A ² are each independently a substituted or unsubstituted aliphatic hydrocarbon group having 1 to 18 carbon atoms, or a substituted or unsubstituted aromatic hydrocarbon group. And A ¹ and A ² may be the same or different.)

Examples of the carbonic acid diester represented by the above formula (3) include substituted diphenyl carbonate such as diphenyl carbonate and ditolyl carbonate, dimethyl carbonate, diethyl carbonate, and di-t-butyl carbonate, preferably diphenyl carbonate. Carbonate and substituted difel carbonate, particularly preferably diphenyl carbonate. Here, “substitution” in relation to the above formula (3) means that the substituent is substituted with a substituent having a molecular weight of 200 or less. Carbonic acid diesters may contain impurities such as chloride ions, which may hinder the polymerization reaction or worsen the hue of the resulting polycarbonate resin. It is preferable to use what was done.

<Transesterification reaction catalyst>
The polycarbonate resin used in the present invention is produced by transesterifying the dihydroxy compound containing the dihydroxy compound used in the present invention with a carbonic acid diester as described above. More specifically, it can be obtained by transesterification and removing by-product monohydroxy compounds and the like out of the system. In this case, polycondensation is usually carried out by transesterification in the presence of a transesterification catalyst.

  The transesterification reaction catalyst (hereinafter simply referred to as a catalyst or a polymerization catalyst) that can be used in the production of the polycarbonate resin used in the present invention can affect the light transmittance at a wavelength of 350 nm and the yellow index value. Therefore, the catalyst that can be used in the present invention is preferably one that can satisfy the weather resistance, that is, the light transmittance at a wavelength of 350 nm and the yellow index that can be set to a predetermined value. A compound containing at least one metal selected from the group consisting of metals belonging to Table 2 is essential in the production of the polycarbonate resin used in the present invention.

  Along with a compound containing at least one metal selected from the group consisting of lithium and long-period periodic table group 2 metals used as a catalyst, a long-period periodic table group 1 metal other than lithium It is also possible to use a basic compound such as a compound containing, a basic boron compound, a basic phosphorus compound, a basic ammonium compound, an amine compound, etc., but a long-period periodic table group 1 metal compound and / or More preferably, only a long-period periodic table group 2 metal compound is used, and only a compound containing at least one metal selected from the group consisting of lithium and a metal of long-period periodic table group 2 is used. Is particularly preferred.

  Moreover, as a form of the compound containing a metal of a long-period type periodic table group 1 or a compound containing a metal of a long-period type periodic table group 2, usually a hydroxide, carbonate, carboxylate, phenol salt, etc. Although used in the form of a salt, hydroxides, carbonates and acetates are preferable from the viewpoint of easy availability and handling, and acetates are preferable from the viewpoint of hue and polymerization activity.

  Lithium hydroxide, lithium hydrogen carbonate, lithium carbonate, lithium acetate, lithium stearate, lithium borohydride, lithium borohydride, lithium benzoate, dilithium hydrogen phosphate, phenyl phosphorus as compounds containing lithium that can be used as a catalyst Examples include dilithium acid, lithium alcoholate or phenolate, and bisphenol A dilithium salt.

Examples of the compound containing a metal of Group 1 of the periodic table other than lithium that can be used as a catalyst include, for example, sodium hydroxide, sodium bicarbonate, sodium carbonate, sodium acetate, sodium stearate, sodium borohydride Sodium borohydride, sodium benzoate, disodium hydrogen phosphate, disodium phenyl phosphate, sodium alcoholate or phenolate, disodium salt of bisphenol A, potassium hydroxide, potassium hydrogen carbonate, carbonic acid Potassium, potassium acetate, potassium stearate, potassium borohydride, potassium phenyl borohydride, potassium benzoate, dipotassium hydrogen phosphate, dipotassium phenyl phosphate, potassium alcoholate or phenolate, bisphenol Potassium compounds such as dipotassium salt of A, cesium hydroxide, cesium bicarbonate, cesium carbonate, cesium acetate, cesium stearate, cesium borohydride, cesium phenyl borohydride, cesium benzoate, 2 cesium hydrogen phosphate, phenyl Examples include cesium compounds such as 2 cesium phosphate, alcoholate or phenolate of cesium, and 2 cesium salt of bisphenol A.

  Examples of the compound containing a metal of Group 2 of the long-period periodic table that can be used as a catalyst include calcium compounds such as calcium hydroxide, calcium hydrogen carbonate, calcium carbonate, calcium acetate, and calcium stearate, barium hydroxide, and hydrogen carbonate. Barium compounds such as barium, barium carbonate, barium acetate and barium stearate, magnesium compounds such as magnesium hydroxide, magnesium bicarbonate, magnesium carbonate, magnesium acetate and magnesium stearate, strontium hydroxide, strontium bicarbonate, strontium carbonate and acetic acid Examples include strontium compounds such as strontium and strontium stearate. Among them, magnesium compounds, calcium compounds and barium compounds are preferable, and the polymerization activity and the polycarbonate obtained. From the viewpoint of the hue of over preparative resin, at least one metal compound is more preferably selected from the group consisting of magnesium compound and calcium compound, most preferably a calcium compound.

  Examples of the basic boron compound include tetramethyl boron, tetraethyl boron, tetrapropyl boron, tetrabutyl boron, trimethylethyl boron, trimethylbenzyl boron, trimethylphenyl boron, triethylmethyl boron, triethylbenzyl boron, triethylphenyl boron, tributylbenzyl. Examples include sodium, potassium, lithium, calcium, barium, magnesium, or strontium salts such as boron, tributylphenylboron, tetraphenylboron, benzyltriphenylboron, methyltriphenylboron, butyltriphenylboron, etc. It is done.

  Examples of the basic phosphorus compound include triethylphosphine, tri-n-propylphosphine, triisopropylphosphine, tri-n-butylphosphine, triphenylphosphine, tributylphosphine, and quaternary phosphonium salts.

  Examples of the basic ammonium compound include tetramethylammonium hydroxide, tetraethylammonium hydroxide, tetrapropylammonium hydroxide, tetrabutylammonium hydroxide, trimethylethylammonium hydroxide, trimethylbenzylammonium hydroxide, trimethylphenylammonium hydroxide, Triethylmethylammonium hydroxide, triethylbenzylammonium hydroxide, triethylphenylammonium hydroxide, tributylbenzylammonium hydroxide, tributylphenylammonium hydroxide, tetraphenylammonium hydroxide, benzyltriphenylammonium hydroxide, methyltriphenylammonium hydroxide Sid, butyl triphenyl ammonium hydroxide, and the like.

  Examples of the amine compound include 4-aminopyridine, 2-aminopyridine, N, N-dimethyl-4-aminopyridine, 4-diethylaminopyridine, 2-hydroxypyridine, 2-methoxypyridine, 4-methoxypyridine, 2 -Dimethylaminoimidazole, 2-methoxyimidazole, imidazole, 2-mercaptoimidazole, 2-methylimidazole, aminoquinoline and the like.

  Among these, in order to make the polycarbonate resin composition of the present invention particularly excellent in transparency, hue, and light sensitivity, the catalyst contains at least one metal selected from the group consisting of magnesium compounds and calcium compounds. It is preferable that it is a compound containing.

The amount of the polymerization catalyst used is usually 0.1 μm per 1 mol of all dihydroxy compounds used.
mol to 300 μmol, preferably 0.5 μmol to 100 μmol, and in particular, when using at least one metal compound selected from the group consisting of lithium and a metal of Group 2 of the long-period periodic table, particularly a magnesium compound and a calcium compound In the case of using at least one metal compound selected from the group consisting of, the amount of metal per 1 mol of all dihydroxy compounds used is usually 0.1 μmol or more, preferably 0.5 μmol or more, particularly preferably 0.7 μmol or more. To do. Further, the upper limit is usually 20 μmol, preferably 10 μmol, more preferably 3 μmol, particularly preferably 1.5 μmol, and most preferably 1.0 μmol.

  If the amount of the catalyst is too small, the polymerization rate is slowed down. As a result, when trying to obtain a polycarbonate resin having a desired molecular weight, the polycondensation temperature must be increased, and the hue and weather resistance of the obtained polycarbonate resin are reduced. The unreacted raw material volatilizes during the polymerization, and the molar ratio of the dihydroxy compound containing the dihydroxy compound used in the present invention to the carbonic acid diester may collapse, and the desired molecular weight may not be reached. On the other hand, when there is too much usage-amount of a polymerization catalyst, the hue of the polycarbonate resin obtained will be deteriorated and the weather resistance of a polycarbonate resin may deteriorate.

  Further, in the polycarbonate resin used in the present invention, metals of Group 1 of the long-period type periodic table, especially sodium, potassium and cesium, are not only from the auxiliary catalyst but also from raw materials such as dihydroxy compounds and reactors. There are cases where these metals are mixed, but if these metals are contained in a large amount in the polycarbonate resin, the hue may be adversely affected. Therefore, the metals are mixed not only from the auxiliary catalyst but also from the raw materials and reactor. Therefore, the total amount of these compounds in the polycarbonate resin is preferably smaller, and the amount of metal is usually 1 ppm by weight or less, preferably 0.8 ppm by weight or less, more preferably 0.7 ppm by weight or less. It is.

  The amount of metal in the polycarbonate resin can be measured by various conventionally known methods. After recovering the metal in the polycarbonate resin by a method such as wet ashing, atomic emission, atomic absorption, Inductively Coupled Plasma (ICP) It can measure using the method of these. In the present invention, it can be considered that all the metal in the polycarbonate resin remains in the polycarbonate resin composition unless an operation for removing a metal such as a catalyst is performed.

<Manufacturing method>
The polycarbonate resin used in the present invention is obtained by polycondensation of a dihydroxy compound containing the dihydroxy compound used in the present invention and a carbonic acid diester by a transesterification reaction. The raw material dihydroxy compound and the carbonic acid diester are converted before the transesterification reaction. It is preferable to mix uniformly.

  The mixing temperature is usually 80 ° C. or higher, preferably 90 ° C. or higher, and the upper limit is usually 250 ° C. or lower, preferably 200 ° C. or lower, more preferably 150 ° C. or lower. Among these, 95 ° C. or higher and 120 ° C. or lower is preferable. If the mixing temperature is too low, the dissolution rate may be slow or the solubility may be insufficient, often causing problems such as solidification, and if the mixing temperature is too high, the dihydroxy compound may be thermally deteriorated. There is a possibility that the hue of the polycarbonate resin obtained will deteriorate and the weather resistance will be adversely affected.

The operation of mixing the dihydroxy compound containing the dihydroxy compound used in the present invention, which is a raw material of the polycarbonate resin used in the present invention, and the carbonic acid diester is an oxygen concentration of 10% by volume or less, further 0.0001% by volume to 10% by volume, From the viewpoint of preventing hue deterioration, it is preferably performed in an atmosphere of 0.0001% by volume to 5% by volume, particularly 0.0001% by volume to 1% by volume.

  In order to obtain the resin of the present invention, the carbonic acid diester is preferably used in a molar ratio of 0.90 to 1.20, more preferably to the total dihydroxy compound including the dihydroxy compound used in the present invention used in the reaction. Is a molar ratio of 0.95 to 1.10. When this molar ratio is decreased, the terminal hydroxyl group of the produced polycarbonate resin is increased, the thermal stability of the polymer is deteriorated, coloring occurs at the time of molding, the rate of transesterification reaction is decreased, and the desired high molecular weight. The body may not be obtained. Moreover, when this molar ratio becomes large, the rate of transesterification may decrease, or it may be difficult to produce a polycarbonate having a desired molecular weight. The decrease in the transesterification reaction rate may increase the heat history during the polymerization reaction, and may deteriorate the hue and weather resistance of the resulting polycarbonate resin.

Furthermore, when the molar ratio of the carbonic acid diester is increased with respect to all the dihydroxy compounds including the dihydroxy compound used in the present invention, the amount of residual carbonic acid diester in the obtained polycarbonate resin increases, and these absorb the ultraviolet rays to absorb the polycarbonate resin. May worsen the weather resistance. The concentration of the carbonic acid diester represented by the formula (3) remaining in the polycarbonate resin used in the present invention is preferably 200 ppm by weight or less, more preferably 100 ppm by weight or less, particularly preferably 60 ppm by weight or less, and particularly 30 wt. ppm or less is preferred. Actually, the polycarbonate resin may contain unreacted carbonic acid diester, and the lower limit of the concentration is usually 1 ppm by weight.

  In the present invention, the method of polycondensing a dihydroxy compound and a carbonic acid diester is usually carried out in multiple stages using a plurality of reactors in the presence of the above-mentioned catalyst. The type of reaction may be any of batch type, continuous type, or a combination of batch type and continuous type.

  In the initial stage of polymerization, it is preferable to obtain a prepolymer at a relatively low temperature and low vacuum, and in the latter stage of polymerization, it is preferable to increase the molecular weight to a predetermined value at a relatively high temperature and high vacuum, but the jacket temperature at each molecular weight stage. It is important from the viewpoint of hue and weather resistance to appropriately select the internal temperature and pressure in the reaction system. For example, if either the temperature or the pressure is changed too quickly before the polymerization reaction reaches a predetermined value, the unreacted monomer will be distilled, causing the molar ratio of the dihydroxy compound and the carbonic acid diester to change, resulting in a decrease in the polymerization rate. May be incurred.

  Furthermore, it is effective to use a reflux condenser for the polymerization reactor in order to suppress the amount of the monomer to be distilled off, and the effect is particularly great in a reactor at the initial stage of polymerization where there are many unreacted monomer components. The temperature of the refrigerant introduced into the reflux cooler can be appropriately selected according to the monomer used. Usually, the temperature of the refrigerant introduced into the reflux cooler is 45 ° C. to 180 ° C. at the inlet of the reflux cooler. Preferably, it is 80 degreeC-150 degreeC, Most preferably, it is 100 degreeC-130 degreeC. If the temperature of the refrigerant is too high, the amount of reflux decreases and the effect is reduced. On the other hand, if the temperature is too low, the distillation efficiency of the monohydroxy compound that should be distilled off tends to decrease. As the refrigerant, hot water, steam, heat medium oil or the like is used, and steam or heat medium oil is preferable.

  In order to maintain the polymerization rate appropriately and suppress the distillation of the monomer, but not to impair the hue, thermal stability, weather resistance, etc. of the final polycarbonate resin, Selection is important.

The polycarbonate resin used in the present invention is preferably produced by polymerizing in a plurality of stages using a plurality of reactors using a catalyst, but the reason for carrying out the polymerization in a plurality of reactors is the initial stage of the polymerization reaction. In order to shift the equilibrium to the polymerization side in the later stage of the polymerization reaction, it is important to suppress the volatilization of the monomer while maintaining the necessary polymerization rate because there are many monomers contained in the reaction solution. This is because it is important to sufficiently distill off the by-produced monohydroxy compound. Thus, in order to set different polymerization reaction conditions, it is preferable from the viewpoint of production efficiency to use a plurality of polymerization reactors arranged in series.

  As described above, the reactor used in the method of the present invention may be at least 2 or more, but from the viewpoint of production efficiency, 3 or more, preferably 3 to 5, more preferably 4 It is a group. In the present invention, if there are two or more reactors, a plurality of reaction stages having different conditions may be provided in the reactor, or the temperature and pressure may be continuously changed.

  In the present invention, the polymerization catalyst can be added to the raw material preparation tank, the raw material storage tank, or can be added directly to the polymerization tank. From the viewpoint of supply stability and polymerization control, the polymerization catalyst is supplied to the polymerization tank. A catalyst supply line is installed in the middle of the raw material line before being fed, and preferably supplied as an aqueous solution.

  If the temperature of the polymerization reaction is too low, the productivity is lowered and the thermal history of the product is increased. If it is too high, not only the monomer is volatilized but also decomposition and coloring of the polycarbonate resin may be promoted.

  Specifically, the reaction in the first stage is performed at 140 to 270 ° C., preferably 180 to 240 ° C., more preferably 200 to 230 ° C. as the maximum internal temperature of the polymerization reactor. The monohydroxy compound generated is removed from the reaction system at a pressure of 10 kPa, preferably 70 kPa to 5 kPa, more preferably 30 kPa to 1 kPa (absolute pressure) for 0.1 hour to 10 hours, preferably 0.5 hour to 3 hours. Carried out while distilling.

  In the second and subsequent stages, the pressure in the reaction system is gradually reduced from the pressure in the first stage, and the monohydroxy compound that is subsequently generated is removed from the reaction system. 200 Pa or less, maximum internal temperature of 210 ° C. to 270 ° C., preferably 220 ° C. to 250 ° C., usually 0.1 hour to 10 hours, preferably 1 hour to 6 hours, particularly preferably 0.5 hour. Perform for ~ 3 hours.

In particular, in order to obtain a polycarbonate resin having good hue and weather resistance by suppressing the coloring and thermal deterioration of the polycarbonate resin, the maximum internal temperature in all reaction stages is less than 250 ° C., particularly 225 ° C. to 245 ° C. preferable. In addition, the lowering of the polymerization rate in the latter half of the polymerization reaction is suppressed,
In order to minimize deterioration due to thermal history, it is preferable to use a horizontal reactor excellent in plug flow property and interface renewability at the final stage of polymerization.

  In order to obtain a polycarbonate resin having a predetermined molecular weight, if the polymerization temperature is increased and the polymerization time is too long, the ultraviolet transmittance decreases and the YI value tends to increase.

The monohydroxy compound produced as a by-product is preferably reused as a raw material for diphenyl carbonate, bisphenol A, etc. after purification as necessary from the viewpoint of effective utilization of resources.

  The polycarbonate resin used in the present invention is usually cooled and solidified after polycondensation as described above, and pelletized with a rotary cutter or the like.

  The method of pelletization is not limited, but it is extracted from the final polymerization reactor in a molten state, cooled and solidified in the form of a strand, and pelletized, or from the final polymerization reactor in a molten state, uniaxial or biaxial extrusion. The resin is supplied to the machine, melt-extruded, cooled and solidified into pellets, or extracted from the final polymerization reactor in a molten state, cooled and solidified in the form of strands, once pelletized, and then uniaxially again Alternatively, a method may be mentioned in which resin is supplied to a biaxial extruder, melt-extruded, cooled and solidified, and pelletized.

  At that time, in the extruder, the residual monomer under reduced pressure devolatilization, and generally known heat stabilizers, neutralizers, UV absorbers, mold release agents, colorants, antistatic agents, lubricants, lubricants, A plasticizer, a compatibilizer, a flame retardant, etc. can be added and kneaded.

  The melt kneading temperature in the extruder depends on the glass transition temperature and molecular weight of the polycarbonate resin, but is usually 150 ° C to 300 ° C, preferably 200 ° C to 270 ° C, more preferably 230 ° C to 260 ° C. When the melt-kneading temperature is lower than 150 ° C., the polycarbonate resin has a high melt viscosity, and the load on the extruder increases, which may reduce the productivity. When the temperature is higher than 300 ° C., the thermal deterioration of the polycarbonate becomes severe, and there is a possibility that the mechanical strength is decreased due to the decrease in the molecular weight, coloring, and gas generation.

  When the polycarbonate resin used in the present invention is produced, it is desirable to install a filter in order to prevent foreign substances from entering. The filter installation position is preferably on the downstream side of the extruder, and the foreign matter removal size (opening) of the filter is preferably 100 μm or less as the filtration accuracy for 99% removal. In particular, in the case of disagreeing with the entry of minute foreign matters for film use etc., it is preferably 40 μm or less, more preferably 10 μm or less.

  Extrusion of the polycarbonate resin used in the present invention is preferably carried out in a clean room having a higher degree of cleanliness than Class 6, more preferably Class 6 as defined in JIS B 9920 (2002), in order to prevent foreign matter from being mixed after extrusion. It is desirable to do.

  Moreover, when cooling the extruded polycarbonate resin into chips, it is preferable to use a cooling method such as air cooling or water cooling. As the air used for air cooling, it is desirable to use air from which foreign substances in the air have been removed in advance with a hepa filter or the like to prevent reattachment of foreign substances in the air. When water cooling is used, it is desirable to use water from which metal in water has been removed with an ion exchange resin or the like, and foreign matter in water has been removed with a filter. The opening of the filter to be used is preferably 10 μm to 0.45 μm as 99% removal filtration accuracy.

<Physical properties>
The molecular weight of the polycarbonate resin used in the present invention thus obtained can be represented by a reduced viscosity, and the reduced viscosity is usually 0.30 dL / g or more, preferably 0.35 dL / g or more, usually 1 .20 dL / g or less, more preferably 1.00 dL / g or less, and still more preferably 0.80 dL / g or less.

If the reduced viscosity of the polycarbonate resin is too low, the mechanical strength of the molded product may be small. If it is too large, the fluidity at the time of molding tends to decrease, and the productivity and moldability tend to decrease.
The reduced viscosity is measured using a Ubbelohde viscometer at a temperature of 20.0 ° C. ± 0.1 ° C., precisely prepared at a polycarbonate concentration of 0.6 g / dL using methylene chloride as a solvent.

  Furthermore, the lower limit of the concentration of the terminal group represented by the following formula (6) of the polycarbonate resin used in the present invention (sometimes referred to as “terminal phenyl group concentration” in this specification) is usually 20 μeq / g, Preferably it is 40 μeq / g, particularly preferably 50 μeq / g, and the upper limit is usually 160 μeq / g, preferably 140 μeq / g, particularly preferably 100 μeq / g.

If the concentration of the end group represented by the above formula (6) is too high, even if the hue at the time of polymerization or at the time of molding is good, the hue after UV exposure may be deteriorated. Stability may be reduced.
In order to control the concentration of the terminal group represented by the above formula (6), in addition to controlling the molar ratio of the carbonic acid diester to the dihydroxy compound containing the dihydroxy compound used in the present invention as the raw material, Examples thereof include a method of controlling the type and amount, the polymerization pressure and the polymerization temperature.

  When the polycarbonate resin used in the present invention is produced using a substituted diphenyl carbonate such as diphenyl carbonate or ditolyl carbonate as the carbonic acid diester represented by the formula (3), the phenol resin and the substituted phenol are by-produced, and the polycarbonate resin Although it is unavoidable that it remains in the interior, phenol and substituted phenol also have an aromatic ring, which absorbs ultraviolet rays and may cause deterioration in weather resistance, as well as causing odor during molding. There is. The polycarbonate resin contains an aromatic monohydroxy compound having an aromatic ring such as by-product phenol of 1000 ppm by weight or more after a normal batch reaction, but from the viewpoint of weather resistance and odor reduction, it is devolatilized. It is preferably 700 ppm by weight or less, more preferably 500 ppm by weight or less, and particularly preferably 300 ppm by weight or less using a horizontal reactor having excellent performance or an extruder with a vacuum vent. However, it is difficult to remove completely industrially, and the lower limit of the content of the aromatic monohydroxy compound in the polycarbonate resin composition is usually 1 ppm by weight.

  These aromatic monohydroxy compounds may naturally have a substituent depending on the raw material used, and may have, for example, an alkyl group having 5 or less carbon atoms.

Further, when the number of moles of hydrogen atoms bonded to the aromatic ring of the polycarbonate resin used in the present invention is X and the number of moles of hydrogen atoms bonded to other than the aromatic ring is Y, the number of moles of hydrogen atoms bonded to the aromatic ring The ratio of the total number of hydrogen atoms to the number of moles is represented by X / (X + Y). However, as described above, since the aromatic ring having the ability to absorb ultraviolet rays may affect the weather resistance, X / (X + Y) is preferably 0.1 or less, more preferably 0.05 or less, particularly preferably 0.02 or less, and preferably 0.01 or less. X / (X + Y) can be quantified by ¹ H-NMR.

  The polycarbonate resin used in the present invention preferably has a light transmittance at a wavelength of 350 nm of a molded product (thickness 3 mm) molded from the polycarbonate resin of 60% or more, more preferably 65% or more, particularly preferably. 70% or more. When the light transmittance at the wavelength is less than 60%, the absorption increases and the weather resistance may deteriorate. The polycarbonate resin used in the present invention preferably has a light transmittance of 30% or more at a wavelength of 320 nm of a molded body (thickness 3 mm flat plate) molded from the polycarbonate resin, more preferably 40% or more, 50% or more is particularly preferable. When the light transmittance at the wavelength is less than 30%, the weather resistance tends to deteriorate.

3. Ultraviolet Absorber The polycarbonate resin composition of the present invention contains 0.005 parts by weight or more and 5 parts by weight or less of an ultraviolet absorber with respect to 100 parts by weight of the polycarbonate resin.

  The content of the ultraviolet absorber is preferably 0.01 parts by weight or more, more preferably 0.05 parts by weight or more with respect to 100 parts by weight of the polycarbonate resin. On the other hand, it is preferably 3 parts by weight or less, and more preferably 1 part by weight or less. If the content of the ultraviolet absorber is too small, the effect of improving the weather resistance due to the inclusion of the ultraviolet absorber is lowered, and if it is too large, there is a risk of appearance failure due to bleeding out of the ultraviolet absorber.

  The ultraviolet absorber is not particularly limited as long as it is a compound having ultraviolet absorbing ability. In the present embodiment, examples of the compound having ultraviolet absorbing ability include organic compounds and inorganic compounds. Of these, organic compounds are preferred because they are easy to ensure affinity with the polycarbonate resin and are easily dispersed uniformly.

  The molecular weight of the organic compound having ultraviolet absorbing ability is not particularly limited, but is usually 200 or more, preferably 250 or more. Also. Usually, it is 600 or less, preferably 450 or less, more preferably 400 or less. If the molecular weight is too small, there is a possibility of causing a decrease in UV resistance performance after long-term use. When the molecular weight is excessively large, there is a possibility that the transparency of the resin composition is lowered after long-term use.

  Preferred ultraviolet absorbers include benzotriazole compounds, benzophenone compounds, triazine compounds, benzoate compounds, salicylic acid phenyl ester compounds, cyanoacrylate compounds, malonic acid ester compounds, oxalic acid anilide compounds, and the like. . Of these, benzotriazole compounds, hydroxybenzophenone compounds, and malonic ester compounds are preferably used. These may be used alone or in combination of two or more.

  More specific examples of the benzotriazole compounds include 2- (2′-hydroxy-3′-methyl-5′-hexylphenyl) benzotriazole, 2- (2′-hydroxy-3′-t-butyl- 5'-hexylphenyl) benzotriazole, 2- (2'-hydroxy-3 ', 5'-di-t-butylphenyl) benzotriazole, 2- (2'-hydroxy-3'-methyl-5'-t -Octylphenyl) benzotriazole, 2- (2'-hydroxy-5'-t-dodecylphenyl) benzotriazole, 2- (2'-hydroxy-3'-methyl-5'-t-dodecylphenyl) benzotriazole, 2- (2′-hydroxy-5′-t-butylphenyl) benzotriazole, methyl-3- (3- (2H-benzotriazol-2-yl ) -5-t-butyl-4-hydroxyphenyl) propionate and the like.

  Examples of the hydroxybenzophenone compounds include 2,2'-dihydroxybenzophenone, 2,2 ', 4,4'-tetrahydroxybenzophenone, 2-hydroxy-4-octoxybenzophenone and the like.

  Examples of the malonic acid ester compounds include 2- (1-arylalkylidene) malonic acid esters, tetraethyl-2,2 ′-(1,4-phenylene-dimethylidene) -bismalonate, and the like.

Examples of the triazine compound include 2- [4-[(2-hydroxy-3-dodecyloxypropyl) oxy] -2-hydroxyphenyl] -4,6-bis (2,4-dimethylphenyl) -1,3. 5-triazine, 2,4-bis (2,4-dimethylphenyl) -6- (2-hydroxy-4-isooctyloxyphenyl) -s-triazine, 2- (4,6-diphenyl-1,3, 5-triazin-2-yl) -5-[(hexyl) oxy] -phenol (manufactured by Ciba Geigy, Tinuvin 1577FF) and the like.

  Examples of the cyanoacrylate compound include ethyl-2-cyano-3,3-diphenyl acrylate, 2'-ethylhexyl-2-cyano-3,3-diphenyl acrylate, and the like.

  Examples of the oxalic acid anilide-based compound include 2-ethyl-2'-ethoxy-oxalanilide (manufactured by Clariant Japan, Sanduvor VSU).

4). Antioxidant The polycarbonate resin composition of the present invention preferably further contains an antioxidant. When an antioxidant is used, it is usually 0.0001 part by weight or more and 1 part by weight or less, preferably 0.0001 part by weight or more and 0.1 part by weight or less, based on 100 parts by weight of the polycarbonate resin. Preferably they are 0.0002 weight part or more and 0.01 weight part or less. When the content of the antioxidant is usually 0.0001 parts by weight or more with respect to 100 parts by weight of the polycarbonate resin, the coloring suppression effect at the time of molding tends to be good, but the content of the antioxidant is 100% by weight of the polycarbonate resin. If the amount exceeds 1 part by weight with respect to parts by weight, the amount of deposits on the mold during injection molding increases or the amount of deposits on the roll increases when forming a film by extrusion molding. The surface appearance may be impaired.

  The antioxidant is preferably at least one selected from the group consisting of phenolic antioxidants, phosphate antioxidants and sulfur antioxidants, and phenolic antioxidants and / or phosphate oxidations. An inhibitor is more preferred.

  Examples of the phenolic antioxidant include pentaerythritol tetrakis (3-mercaptopropionate), pentaerythritol tetrakis (3-laurylthiopropionate), glycerol-3-stearylthiopropionate, triethylene glycol-bis [ 3- (3-tert-butyl-5-methyl-4-hydroxyphenyl) propionate], 1,6-hexanediol-bis [3- (3,5-di-tert-butyl-4-hydroxyphenyl) propionate] , Pentaerythritol-tetrakis [3- (3,5-di-tert-butyl-4-hydroxyphenyl) propionate], octadecyl-3- (3,5-di-tert-butyl-4-hydroxyphenyl) propionate, 1 , 3,5-trimethyl-2 4,6-tris (3,5-di-tert-butyl-4-hydroxybenzyl) benzene, N, N-hexamethylenebis (3,5-di-tert-butyl-4-hydroxy-hydrocinnamide), 3,5-di-tert-butyl-4-hydroxy-benzylphosphonate-diethyl ester, tris (3,5-di-tert-butyl-4-hydroxybenzyl) isocyanurate, 4,4′-biphenylenediphosphinic acid tetrakis ( 2,4-di-tert-butylphenyl), 3,9-bis {1,1-dimethyl-2- [β- (3-tert-butyl-4-hydroxy-5-methylphenyl) propionyloxy] ethyl} And compounds such as -2,4,8,10-tetraoxaspiro (5,5) undecane.

Among these compounds, an aromatic monohydroxy compound substituted with one or more alkyl groups having 5 or more carbon atoms is preferable. Specifically, octadecyl-3- (3,5-di-tert-butyl-4- Hydroxyphenyl) propionate, pentaerythrityl-tetrakis {3- (3,5-di-t-butyl-4-hydroxyphenyl) propionate}, 1,6-hexanediol-bis [3- (3,5-di- tert-butyl-4-hydroxyphenyl) propionate], 1,3,5-trimethyl-2,4,6-tris (3,5-di-tert-butyl-4-hydroxybenzyl) benzene and the like, preferably pentaerythris Lithyl-tetrakis {3- (3,5-di-t-butyl-4-hydroxyphenyl) propionate is more preferred.

  Examples of the phosphate antioxidant include triphenyl phosphite, tris (nonylphenyl) phosphite, tris (2,4-di-tert-butylphenyl) phosphite, tridecyl phosphite, trioctyl phosphite, tri Octadecyl phosphite, didecyl monophenyl phosphite, dioctyl monophenyl phosphite, diisopropyl monophenyl phosphite, monobutyl diphenyl phosphite, monodecyl diphenyl phosphite, monooctyl diphenyl phosphite, bis (2,6-di-tert -Butyl-4-methylphenyl) pentaerythritol diphosphite, 2,2-methylenebis (4,6-di-tert-butylphenyl) octyl phosphite, bis (nonylphenyl) pentaeri Li diphosphite, bis (2,4-di -tert- butylphenyl) pentaerythritol diphosphite, distearyl pentaerythritol diphosphite, and the like.

  Among these, trisnonylphenyl phosphite, trimethyl phosphate, tris (2,4-di-tert-butylphenyl) phosphite, bis (2,4-di-tert-butylphenyl) pentaerythritol diphosphite, bis ( 2,6-di-tert-butyl-4-methylphenyl) pentaerythritol diphosphite is preferred, and tris (2,4-di-tert-butylphenyl) phosphite is more preferred.

  Examples of the sulfur-based antioxidant include dilauryl-3,3′-thiodipropionate, ditridecyl-3,3′-thiodipropionate, dimyristyl-3,3′-thiodipropionate, diester Stearyl-3,3′-thiodipropionate, laurylstearyl-3,3′-thiodipropionate, pentaerythritol tetrakis (3-laurylthiopropionate), bis [2-methyl-4- (3 -Laurylthiopropionyloxy) -5-tert-butylphenyl] sulfide, octadecyl disulfide, mercaptobenzimidazole, 2-mercapto-6-methylbenzimidazole, 1,1′-thiobis (2-naphthol) and the like. Among the above, pentaerythritol tetrakis (3-lauryl thiopropionate) is preferable.

5. Other components The polycarbonate resin composition of the present invention may further contain an acidic compound. When an acidic compound is used, the compounding amount of the acidic compound is 0.00001 part by weight or more and 0.1 part by weight or less, preferably 0.0001 part by weight based on 100 parts by weight of the polycarbonate resin. Part to 0.01 part by weight, more preferably 0.0002 part to 0.001 part by weight. When the compounding amount of the acidic compound is 0.00001 parts by weight or more with respect to 100 parts by weight of the polycarbonate resin, it is possible to suppress coloration when the residence time of the polycarbonate resin composition in the injection molding machine becomes long during injection molding. Although it is preferable at a point, when the compounding quantity of an acidic compound is more than 0.1 weight part with respect to 100 weight part of polycarbonate resin, the hydrolysis resistance of a polycarbonate resin composition may fall.

Examples of acidic compounds include hydrochloric acid, nitric acid, boric acid, sulfuric acid, sulfurous acid, phosphoric acid, phosphorous acid, hypophosphorous acid, polyphosphoric acid, adipic acid, ascorbic acid, aspartic acid, azelaic acid, adenosine phosphoric acid, benzoic acid Acid, formic acid, valeric acid, citric acid, glycolic acid, glutamic acid, glutaric acid, cinnamic acid, succinic acid, acetic acid, tartaric acid, oxalic acid, p-toluenesulfinic acid, p-toluenesulfonic acid, naphthalenesulfonic acid, nicotinic acid , Bronsted acids such as picric acid, picolinic acid, phthalic acid, terephthalic acid, propionic acid, benzenesulfinic acid, benzenesulfonic acid, malonic acid, maleic acid, and esters thereof. Among these acidic compounds or derivatives thereof, sulfonic acids or esters thereof are preferable, and p-toluenesulfonic acid, methyl p-toluenesulfonate, and butyl p-toluenesulfonate are particularly preferable.

  These acidic compounds can be added in the manufacturing process of a polycarbonate resin composition as a compound which neutralizes the basic transesterification catalyst used in the polycondensation reaction of the polycarbonate resin mentioned above.

  A release agent can be blended with the polycarbonate resin composition of the present invention as long as the object of the present invention is not impaired. Although it does not specifically limit as a mold release agent, A higher fatty acid, a stearic acid ester, etc. are mentioned, Preferably it is a higher fatty acid.

  As the higher fatty acid, a substituted or unsubstituted saturated fatty acid having 10 to 30 carbon atoms is preferable. As such a saturated fatty acid, myristic acid, lauric acid, palmitic acid, stearic acid, behenic acid and the like are more preferable. Of these, palmitic acid and stearic acid are more preferable, and stearic acid is particularly preferable.

  As the stearic acid ester, a partial or total ester of a substituted or unsubstituted monovalent or polyhydric alcohol having 1 to 20 carbon atoms and stearic acid is preferable. Examples of partial esters or total esters of monohydric or polyhydric alcohols and stearic acid include stearic acid monoglyceride, stearic acid diglyceride, stearic acid triglyceride, stearic acid monosorbate, stearyl stearate, pentaerythritol monostearate, pentaerythritol. Tetrastearate, propylene glycol monostearate, stearyl stearate, butyl stearate, sorbitan monostearate, 2-ethylhexyl stearate and the like are more preferable. Of these, stearic acid monoglyceride, stearic acid triglyceride, pentaerythritol tetrastearate and stearyl stearate are more preferable, and stearic acid monoglyceride and stearyl stearate are particularly preferable.

  One of these release agents may be used alone, or two or more thereof may be mixed and used. The compounding amount of the release agent is 0 to 2 parts by weight, preferably 0.01 to 1 part by weight, and more preferably 0.1 to 0 part by weight with respect to 100 parts by weight of the polycarbonate resin. .5 parts by weight. If the release agent content is excessively large, mold deposits may increase at the time of molding. If a large amount of molding is performed, it may require labor to maintain the molding machine. When the molding agent content is 0.0001 parts by weight or more with respect to 100 parts by weight, which may cause poor appearance, the molded product will be easily released from the mold during molding. There is an advantage that it is easy to do.

  In the present embodiment, the addition timing and addition method of the release agent are not particularly limited. For example, when the polycarbonate resin is produced by the transesterification method, when the polymerization reaction is completed; the polycarbonate resin melted during mixing of the polycarbonate resin and other compounding agents regardless of the polymerization method. A case where it is blended and kneaded with a polycarbonate resin in a solid state such as pellets or powder using an extruder or the like. As an addition method, a release agent may be directly mixed or kneaded with a polycarbonate resin; a high-concentration master batch prepared using a release agent with a small amount of a polycarbonate resin or other resin may be added.

  A flame retardant can be blended in the polycarbonate resin composition of the present invention as long as the object of the present invention is not impaired. The blending amount of the flame retardant can be appropriately selected according to the type of flame retardant and the degree of flame retardancy. In the present invention, the flame retardant is 0 to 30 parts by weight with respect to 100 parts by weight of the polycarbonate. It is.

  Examples of the flame retardant include phosphorus-containing compound flame retardants, halogen-containing compound flame retardants, sulfonic acid metal salt flame retardants, and silicon-containing compound flame retardants. In the present embodiment, at least one selected from these groups can be used. These may be used alone or in combination of two or more.

  Examples of the phosphorus-containing compound flame retardant include phosphate ester compounds, phosphazene compounds, red phosphorus, coated red phosphorus, polyphosphate compounds, and the like. The compounding quantity of a phosphorus containing compound type flame retardant is 0 weight part-20 weight part with respect to 100 weight part of polycarbonate. If the amount is too large, the heat resistance tends to decrease.

  Examples of the halogen-containing compound flame retardant include tetrabromobisphenol A, tribromophenol, brominated aromatic triazine, tetrabromobisphenol A epoxy oligomer, tetrabromobisphenol A epoxy polymer, decabromodiphenyl oxide, tribromoallyl ether, Examples thereof include tetrabromobisphenol A carbonate oligomer, ethylenebistetrabromophthalimide, decabromodiphenylethane, brominated polystyrene, and hexabromocyclododecane.

  The blending amount of the halogen-containing compound flame retardant is 0 to 20 parts by weight with respect to 100 parts by weight of the polycarbonate resin. If the blending amount of the halogen-containing compound-based flame retardant is excessively large, the mechanical strength is lowered, and the flame retardant may cause discoloration due to bleeding.

  Examples of the sulfonic acid metal salt-based flame retardant include an aliphatic sulfonic acid metal salt, an aromatic sulfonic acid metal salt, a perfluoroalkane-sulfonic acid metal salt, and the like. Preferred examples of the metal of these metal salts include metals of Group 1 of the periodic table, metals of Group 2 of the periodic table, and the like. Specifically, alkali metals such as lithium, sodium, potassium, rubidium and cesium; alkaline earth metals such as calcium, strontium and barium; beryllium and magnesium.

  Among the sulfonic acid metal salt flame retardants, aromatic sulfonesulfonic acid metal salts, perfluoroalkane-sulfonic acid metal salts, and the like are preferable from the viewpoints of flame retardancy and thermal stability. The aromatic sulfonesulfonic acid metal salt is preferably an aromatic sulfonesulfonic acid alkali metal salt or an aromatic sulfonesulfonic acid alkaline earth metal salt. These may be polymers. Specific examples of the aromatic sulfonesulfonic acid metal salt include sodium salt of diphenylsulfone-3-sulfonic acid, potassium salt of diphenylsulfone-3-sulfonic acid, and 4,4′-dibromodiphenyl-sulfone-3-sulfone. Sodium salt of acid, potassium salt of 4,4′-dibromodiphenyl-sulfone-3-sulfone, calcium salt of 4-chloro-4′-nitrodiphenylsulfone-3-sulfonic acid, diphenylsulfone-3,3′-disulfonic acid And the dipotassium salt of diphenylsulfone-3,3′-disulfonic acid.

  The perfluoroalkane-sulfonic acid metal salt is preferably an alkali metal salt of perfluoroalkane-sulfonic acid, an alkaline earth metal salt of perfluoroalkane-sulfonic acid, or the like. Furthermore, a sulfonic acid alkali metal salt having a C 4-8 perfluoroalkane group, a sulfonic acid alkaline earth metal salt having a C 4-8 perfluoroalkane group, and the like are more preferable.

Specific examples of the perfluoroalkane-sulfonic acid metal salt include, for example, perfluorobutane-sodium sulfonate, perfluorobutane-potassium sulfonate, perfluoromethylbutane-sodium sulfonate, perfluoromethylbutane-potassium sulfonate, Examples include perfluorooctane-sodium sulfonate, potassium perfluorooctane-sulfonate, and tetraethylammonium salt of perfluorobutane-sulfonate.

  The compounding quantity of a sulfonic-acid metal salt type flame retardant is 0-5 weight part with respect to 100 weight part of polycarbonate. If the amount of the sulfonic acid metal salt flame retardant is excessively large, the thermal stability tends to be lowered.

  Examples of the silicon-containing compound flame retardant include silicone varnish, a silicone resin in which a substituent bonded to a silicon atom is an aromatic hydrocarbon group and an aliphatic hydrocarbon group having 2 or more carbon atoms, and a main chain having a branched structure. And a silicone compound having an aromatic group in the organic functional group contained therein, a silicone powder carrying a polydiorganosiloxane polymer which may have a functional group on the surface of the silica powder, and an organopolysiloxane-polycarbonate copolymer Etc. Of these, silicone varnish is preferred.

As the silicone varnish, for example, mainly composed of a bifunctional unit [R ⁰ ₂ SiO] and a trifunctional unit [R ⁰ SiO _1.5 ], a monofunctional unit [R ⁰ ₃ SiO _0.5 ] and / or A relatively low molecular weight solution-like silicone resin that may contain tetrafunctional units [SiO ₂ ] may be mentioned. Here, R ⁰ is a C 1-12 hydrocarbon group or a C 1-12 hydrocarbon group substituted with one or more substituents. Examples of the substituent include an epoxy group, an amino group, a hydroxyl group, and a vinyl group. By changing the type of R ^0, the compatibility with the matrix resin can be improved.

  Examples of the silicone varnish include a solventless silicone varnish and a silicone varnish containing a solvent. In the present embodiment, a silicone varnish containing no solvent is preferable. The silicone varnish can be produced, for example, by hydrolysis of alkylalkoxysilanes such as alkyltrialkoxysilanes, dialkyldialkoxysilanes, trialkylalkoxysilanes, and tetraalkoxysilanes. The molecular structure (crosslinking degree) and molecular weight can be controlled by adjusting the molar ratio of these raw materials, the hydrolysis rate, and the like. Furthermore, although alkoxysilane remains depending on the production conditions, if it remains in the composition, the hydrolysis resistance of the polycarbonate resin may be lowered.

The viscosity of the silicone varnish is preferably 300 centistokes or less, more preferably 250 centistokes or less, and still more preferably 200 centistokes or less. If the viscosity of the silicone varnish is excessively large, flame retardancy may be insufficient.
The compounding quantity of a silicon-containing compound type flame retardant is 0-10 weight part with respect to 100 weight part of polycarbonate resin. When the compounding amount of the silicon-containing compound flame retardant is excessively large, the heat resistance tends to be lowered.

  In order to achieve higher flame retardancy, the combined use of polytetrafluoroethylene for preventing dripping is preferable. Anti-dripping polytetrafluoroethylene tends to disperse easily in the polymer and bind the polymers together to produce a fibrous material. Examples of commercially available products for preventing dripping include Teflon (registered trademark) 6J, Teflon (registered trademark) 30J (Mitsui / DuPont Roro Chemical Co., Ltd.), Polyflon F201L (Daikin Chemical Industry Co., Ltd.) and the like.

The amount of polytetrafluoroethylene for preventing dripping is preferably more than 0 parts by weight and 2.0 parts by weight or less with respect to 100 parts by weight of the polycarbonate resin. When the blending amount of polytetrafluoroethylene for dripping prevention is excessively small, the effect of preventing melt dripping at the time of combustion is insufficient, and when it is excessively large, the appearance of the molded product tends to deteriorate.

  In this Embodiment, the addition time of the flame retardant mix | blended with polycarbonate resin and the addition method are not specifically limited. For example, when the polycarbonate resin is produced by the transesterification method, when the polymerization reaction is completed; the polycarbonate resin melted during mixing of the polycarbonate resin and other compounding agents regardless of the polymerization method. A case where it is blended and kneaded with a polycarbonate resin in a solid state such as pellets or powder using an extruder or the like. As the addition method, a filler can be directly mixed or kneaded with a polycarbonate resin; it can also be added as a high-concentration masterbatch prepared using a small amount of a polycarbonate resin or other resin and the filler.

  A filler can be blended in the polycarbonate resin composition of the present invention as long as the object of the present invention is not impaired. Examples of the filler that can be blended in the polycarbonate resin composition of the present invention include inorganic fillers and organic fillers.

  The blending amount of the filler is 0 to 100 parts by weight with respect to 100 parts by weight of the polycarbonate resin. The blending amount of the filler is preferably 50 parts by weight or less, more preferably 40 parts by weight or less, and still more preferably 35 parts by weight or less. Although the reinforcing effect of the polycarbonate resin composition can be obtained by blending the filler, the appearance tends to be deteriorated when blending more than 100 parts by weight.

  Examples of the inorganic filler include glass fiber, glass milled fiber, glass flake, glass bead, silica, alumina, titanium oxide, calcium sulfate powder, gypsum, gypsum whisker, barium sulfate, talc, mica, wollastonite and the like. Calcium silicate: carbon black, graphite, iron powder, copper powder, molybdenum disulfide, silicon carbide, silicon carbide fiber, silicon nitride, silicon nitride fiber, brass fiber, stainless steel fiber, potassium titanate fiber, whisker and the like. Among these, glass fiber filler, glass powder filler, glass flake filler; various whiskers, mica and talc are preferable. More preferably, glass fiber, glass flake, glass milled fiber, wollastonite, mica and talc are mentioned. Particularly preferred is at least one selected from glass fiber and talc. Although the inorganic filler mentioned above can also be used only by 1 type, it can also be used in combination of 2 or more type.

  Among inorganic fillers, any glass fiber or glass milled fiber may be used as long as it is used in thermoplastic resins. In particular, alkali-free glass (E glass) is preferable. The diameter of glass fiber becomes like this. Preferably they are 6 micrometers-20 micrometers, More preferably, they are 9 micrometers-14 micrometers. If the diameter of the glass fiber is too small, the reinforcing effect tends to be insufficient. On the other hand, if it is excessively large, the product appearance is liable to be adversely affected.

The glass fiber is preferably chopped strands cut to a length of 1 mm to 6 mm; preferably glass milled fibers that are commercially available after being pulverized to a length of 0.01 mm to 0.5 mm. You may use these individually or in mixture of both.
The glass fiber used in the present invention is made of an acrylic resin or urethane to improve surface treatment with a silane coupling agent such as aminosilane or epoxysilane, or to improve handling properties, in order to improve adhesion to the polycarbonate resin. It may be used after being subjected to a focusing treatment with a resin or the like.

Any glass beads can be used as long as they are used in thermoplastic resins. Among these, alkali-free glass (E glass) is preferable. The shape of the glass beads is preferably spherical with a particle size of 10 μm to 50 μm.
As glass flakes, scaly glass flakes can be mentioned. The maximum diameter of the glass flake after blending the polycarbonate resin is generally 1000 μm or less, preferably 1 μm to 500 μm, and the aspect ratio (the ratio of the maximum diameter to the thickness) is 5 or more, preferably 10 or more, Preferably it is 30 or more.

  Examples of organic fillers include powdery organic fillers such as wood powder, bamboo powder, coconut starch, and pulp powder; balun-like and spherical organic fillers such as crosslinked polyester, polystyrene, styrene / acrylic copolymer, and urea resin. And fibrous organic fillers such as carbon fiber, synthetic fiber and natural fiber.

  The carbon fiber is not particularly limited, and is produced by firing using, for example, acrylic fiber, petroleum or carbon-based special pitch, cellulose fiber, lignin or the like as a raw material, such as flame resistance, carbonaceous, and graphite. There are various types. The average of the aspect ratio (fiber length / fiber diameter) of the carbon fibers is preferably 10 or more, more preferably 50 or more. If the average aspect ratio is too small, the conductivity, strength, and rigidity of the polycarbonate resin composition tend to be reduced. The diameter of the carbon fiber is 3 μm to 15 μm, and any shape such as chopped strand, roving strand, milled fiber, etc. can be used to adjust the aspect ratio. Carbon fiber can be used 1 type or in mixture of 2 or more types.

  As long as the properties of the polycarbonate resin composition of the present invention are not impaired, the carbon fiber may be subjected to surface treatment such as epoxy treatment, urethane treatment, oxidation treatment, etc., in order to increase the affinity with the polycarbonate resin.

  In this Embodiment, the addition time of the filler mix | blended with polycarbonate resin and the addition method are not specifically limited. For example, when the polycarbonate resin is produced by the transesterification method, when the polymerization reaction is completed; the polycarbonate resin melted during mixing of the polycarbonate resin and other compounding agents regardless of the polymerization method. A case where it is blended and kneaded with a polycarbonate resin in a solid state such as pellets or powder using an extruder or the like. As an addition method, a method of directly mixing or kneading an inorganic filler to a polycarbonate resin; a high-concentration masterbatch prepared using a small amount of a polycarbonate resin or other resin and an inorganic filler can also be added.

  In the polycarbonate resin composition of the present invention, a bluing agent can be blended in order to counteract the yellowishness of the lens based on the polymer or the ultraviolet absorber. As the bluing agent, any conventional bluing agent can be used as long as it is used for polycarbonate resin. In general, anthraquinone dyes are preferred because they are readily available.

As a specific bluing agent, for example, the general name Solvent Violet 13 [CA. No (color index No) 60725], generic name Solvent Violet 31 [CA. No 68210], common name Solvent Violet 33 [CA. No. 60725], generic name Solvent Blue 94 [CA. No 61500], generic name Solvent Violet 36 [CA. No. 68210], general name Solvent Blue 97 [manufactured by Bayer "Macrolex Violet RR"], general name Solvent Blue 45 [CA. No. 61110] and the like are given as representative examples. These bluing agents may be used individually by 1 type, and may use 2 or more types together. These blueing agents are usually blended at a ratio of 0.1 × 10 ⁻⁵ to 2 × 10 ⁻⁴ parts by weight when the polycarbonate resin is 100 parts by weight.

The polycarbonate resin composition of the present invention can contain a light stabilizer as long as the object of the present invention is not impaired. The content of the stabilizer is usually 0 to 2 parts by weight with respect to 100 parts by weight of the polycarbonate resin.

  The polycarbonate resin composition of the present invention can be produced by mixing the above components simultaneously or in any order with a mixer such as a tumbler, V-type blender, nauter mixer, Banbury mixer, kneading roll, or extruder. . Furthermore, nucleating agents, impact modifiers, foaming agents, dyes and the like that are usually used in the resin composition may be included within the range not impairing the object of the present invention.

  In addition, the polycarbonate resin composition of the present invention includes, for example, aromatic polycarbonate, aromatic polyester, aliphatic polyester, polyamide, polystyrene, polyolefin, acrylic, amorphous polyolefin, ABS resin, AS and other synthetic resins, polylactic acid, polybutylene It can also be used as a polymer alloy by kneading with one or more of biodegradable resins such as succinate and rubber.

6). Polycarbonate resin molded product In the present embodiment, a polycarbonate resin molded product obtained by molding the above-described polycarbonate resin composition is obtained. The molding method of the polycarbonate resin molded product is not particularly limited, but the injection molding method is preferable from the viewpoint of the degree of freedom of the molded product shape.

  EXAMPLES Hereinafter, although an Example demonstrates this invention further in detail, this invention is not limited by a following example, unless the summary is exceeded. In addition, the values of various production conditions and evaluation results in the following examples have meanings as preferable values of the upper limit or the lower limit in the embodiment of the present invention, and the preferable range is the above-described upper limit or lower limit value. A range defined by a combination of values of the following examples or values of the examples may be used. In the following, the physical properties and characteristics of the polycarbonate resin and the resin composition were evaluated by the following methods.

1) Measurement of oxygen concentration
The oxygen concentration in the polymerization reaction apparatus was measured using an oxygen meter (manufactured by AMI: 1000RS).

2) Measurement of reduced viscosity
A polycarbonate resin sample was dissolved using methylene chloride as a solvent to prepare a polycarbonate solution having a concentration of 0.6 g / dL. Measured at a temperature of 20.0 ° C. ± 0.1 ° C. using an Ubbelohde viscometer manufactured by Moriyu Rika Kogyo Co., Ltd., and the relative viscosity η _rel is obtained from the following equation from the passage time t _{0 of the} solvent and the passage time t of the solution. ,
η _rel = t / t ₀
From the relative viscosity, the specific viscosity η _sp was determined from the following equation.
η _sp = (η−η ₀ ) / η ₀ = η _rel −1
The reduced viscosity η _sp / c was determined by dividing the specific viscosity by the concentration c (g / dL). The higher this value, the higher the molecular weight.

3) Measurement of structural unit ratio derived from each dihydroxy compound in polycarbonate resin and concentration of terminal phenyl group The ratio of each dihydroxy compound structural unit in polycarbonate resin was measured by weighing 30 mg of polycarbonate resin and dissolved in about 0.7 mL of deuterated chloroform. The solution was put into an NMR tube having an inner diameter of 5 mm, and a ¹ H NMR spectrum was measured at room temperature using JNM-AL400 (resonance frequency 400 MHz) manufactured by JEOL Ltd. The structural unit ratio derived from each dihydroxy compound was determined from the signal intensity ratio based on the structural unit derived from each dihydroxy compound.
The terminal phenyl group concentration was determined from the signal intensity ratio based on the internal standard and the terminal phenyl group by measuring ¹ H-NMR in the same manner as described above using 1,1,2,2-tetrabromoethane as the internal standard.

4) Measurement of metal concentration in polycarbonate resin and metal content in polycarbonate resin composition About 0.5 g of polycarbonate resin pellets were accurately weighed in a microwave decomposition container manufactured by PerkinElmer, and 2 mL of 97% sulfuric acid was added and sealed. Then, microwave heating was performed at 230 ° C. for 10 minutes. After cooling to room temperature, 1.5 mL of 68% nitric acid is added, sealed and microwave heated at 150 ° C. for 10 minutes, cooled again to room temperature, added with 2.5 mL of 68% nitric acid, and sealed again. And microwaved at 230 ° C. for 10 minutes to completely decompose the contents. After cooling to room temperature, the liquid obtained above was diluted with pure water and quantified with ICP-MS manufactured by ThermoQuest.
Based on the metal concentration in the polycarbonate resin determined by the above measurement, the metal content in the entire polycarbonate resin composition was calculated. In the calculation method, first, the weight part of calcium relative to the polycarbonate resin was determined from the molecular weight of each raw material, the formula weight of the catalyst, and the molar ratio of each raw material and catalyst, and then the weight part (ppm by weight) relative to the polycarbonate resin.

5) Measurement of content of aromatic monohydroxy compound in polycarbonate resin, content of carbonic acid diester represented by the above formula (3) After dissolving 1.25 g of polycarbonate resin sample in 7 ml of methylene chloride to make a solution, the total amount is 25 ml. Acetone was added so that a reprecipitation treatment was performed. Next, the treatment liquid was filtered through a 0.2 μm disk filter and quantified by liquid chromatography.

6) Ratio of moles X of hydrogen atoms bonded to the aromatic ring to moles X + Y of all hydrogen atoms (where Y is the number of moles of hydrogen atoms bonded to other than the aromatic ring)
The spectrum of only deuterated chloroform to which tetramethylsilane (TMS) has been added and mixed in advance as an internal standard substance is measured, and the signal ratio of residual hydrogen atoms contained in TMS and deuterated chloroform is determined. Next, 30 mg of polycarbonate resin was weighed and dissolved in about 0.7 mL of the deuterated chloroform. This was put into an NMR tube having an inner diameter of 5 mm, and a ¹ H NMR spectrum was measured at room temperature using JNM-AL400 (resonance frequency 400 MHz) manufactured by JEOL Ltd. From the integrated value of the signal appearing at 6.5 ppm to 8.0 ppm in the obtained NMR chart, the integrated value of the signal of the residual hydrogen atom contained in deuterated chloroform (the integrated value of the TMS signal and the previously determined TMS and The value obtained by subtracting (determined from the ratio to the residual hydrogen atoms contained in deuterated chloroform) is x. On the other hand, when the integral value of the signal appearing at 0.5 ppm to 6.5 ppm is y, x / (x + y) = X / (X + Y), and thus this was obtained.

7) Measurement of light transmittance at wavelengths of 350 nm and 320 nm Polycarbonate resin pellets were dried at 110 ° C. for 10 hours in a nitrogen atmosphere. Next, the dried polycarbonate resin pellets are supplied to an injection molding machine (J75EII type, manufactured by Nippon Steel Co., Ltd.), and an injection molded piece (width 60 mm × length 60 mm) under the conditions of a resin temperature of 220 ° C. and a molding cycle of 23 seconds. × Thickness 3 mm) was molded, and the light transmittance in the thickness direction was measured using an ultraviolet-visible spectrophotometer (U2900 manufactured by Hitachi High-Technologies Corporation), and the average value was calculated and evaluated.

8) Method for evaluating initial hue of polycarbonate resin composition The pellets of the polycarbonate resin composition were dried at 110 ° C for 10 hours in a nitrogen atmosphere. Next, the pellets of the dried polycarbonate resin composition were supplied to an injection molding machine (J75EII type manufactured by Nippon Steel Co., Ltd.), and injection molded pieces (width 60 mm × length) under the conditions of a resin temperature of 220 ° C. and a molding cycle of 23 seconds. The yellow index (initial YI) value in the transmitted light with respect to the square surface of the injection-molded pieces obtained in the 10th to 20th shots is repeated using a color tester (Konica Minolta). The average value was calculated using CM-3700d). The smaller the YI value, the better the quality without yellowness.

9) Evaluation method of initial haze (cloudiness value) of polycarbonate resin composition According to JIS K7105, the above injection-molded piece (width 60 mm × length 60 mm × thickness 3 mm) was measured using a haze meter, and the average value was calculated. Calculated. The smaller the value, the better the transparency.

10) Metal halide lamp accelerated weathering test Using a metal ring weather meter M6T manufactured by Suga Test Instruments Co., Ltd., a horizontal metal ring lamp as the light source, quartz as the inner filter, and 63 ° C. and 50% relative humidity. A # 500 filter is attached as an outer filter around the lamp, and the irradiance of wavelength 300 nm to 400 nm is set to 1.5 kw / m ^{2. The} 20th shot flat plate obtained in 8) above (width 60 mm × A square surface having a length of 60 mm and a thickness of 3 mm was subjected to an irradiation treatment for 400 hours under a rain spray condition of 12 minutes / 60 minutes. The YI value after treatment was measured in the same manner as in 8) above, and the haze (cloudiness value) after treatment was measured in the same manner as in 9) above.

The abbreviations of the compounds used in the description of the following examples are as follows.
ISB: Isosorbide (Rocket Fleure, trade name POLYSORB)
CHDM: 1,4-cyclohexanedimethanol (Nippon Rika Co., Ltd., SKY C
HDM)
DPC: Diphenyl carbonate (Mitsubishi Chemical Corporation)
(UV absorber)
SEESORB 709: 2- (2′-hydroxy-3′-methyl-5′-t-octylphenyl) benzotriazole (manufactured by Cypro Kasei Co., Ltd.)
SEESORB 102: 2-hydroxy-4-octoxybenzophenone (manufactured by Cypro Kasei Co., Ltd.)
Hostavin B-CAP: Tetraethyl-2,2 ′-(1,4-phenylene-dimethylidene) -bismalonate (manufactured by Clariant Japan KK)
(Antioxidant)
Irganox (registered trademark) 1010: pentaerythrityl-tetrakis {3- (3,5-di-t-butyl-4-hydroxyphenyl) propionate (manufactured by BASF Japan Ltd.)
Irgaphos (registered trademark) 168: Tris (2,4-di-tertbutylphenyl) phosphite (manufactured by BASF Japan Ltd.)

[Example 1]
In a polymerization reactor equipped with a stirring blade and a reflux condenser controlled at 100 ° C., ISB and CHDM, DPC and calcium acetate monohydrate having a chloride ion concentration of 10 ppb or less by purification by distillation, in a molar ratio. ISB / CHDM / DPC / calcium acetate monohydrate = 0.69 / 0.31 / 1.00 / 1.3 × 10 ⁻⁶ , and sufficiently purged with nitrogen (oxygen concentration 0.0005 vol. % To 0.001% by volume). Subsequently, heating was performed with a heating medium, and stirring was started when the internal temperature reached 100 ° C., and the contents were melted and made uniform while controlling the internal temperature to be 100 ° C. After that, temperature increase was started, the internal temperature was adjusted to 210 ° C. in 40 minutes, and when the internal temperature reached 210 ° C., control was performed so as to maintain this temperature, and at the same time, pressure reduction was started and the temperature reached 210 ° C. After 90 minutes, the pressure was changed to 13.3 kPa (absolute pressure, the same applies hereinafter), and the pressure was maintained for another 60 minutes. The phenol vapor produced as a by-product with the polymerization reaction is led to a reflux condenser using a steam controlled at 100 ° C. as the inlet temperature to the reflux condenser, and a monomer component contained in the phenol vapor in a slight amount is introduced into the polymerization reactor. Then, the phenol vapor that did not condense was recovered by guiding it to a condenser using 45 ° C. warm water as a refrigerant.

  The content thus oligomerized is once restored to atmospheric pressure, and then transferred to another polymerization reaction apparatus equipped with a stirring blade and a reflux condenser controlled in the same manner as described above. The internal temperature was set to 220 ° C. and the pressure was set to 200 Pa in 60 minutes. Thereafter, the internal temperature was 228 ° C. and the pressure was 133 Pa or less over 20 minutes, and when the predetermined stirring power was reached, the pressure was restored, and a molten polycarbonate resin was obtained from the outlet of the polymerization reactor.

  Furthermore, the molten polycarbonate resin was continuously supplied to a twin screw extruder equipped with 3 vents and water injection equipment, and “SEESORB 709” as an ultraviolet absorber and an antioxidant as 100 parts by weight of the polycarbonate resin. "Irganox (registered trademark) 1010" and "Irgafos (registered trademark) 168" are continuously added at the prescribed ratios shown in Table 1, and phenol is added to each vent portion provided in the twin-screw extruder. A low molecular weight product such as the above was devolatilized under reduced pressure, and then pelletized with a pelletizer to obtain a polycarbonate resin composition. Various physical properties and the like were evaluated by the evaluation methods described above. The obtained results are shown in Table-1.

[Examples 2 and 3]
The same procedure as in Example 1 was performed except that the type of the ultraviolet absorber in Example 1 was changed.

[Comparative Example 1]
The same procedure as in Example 1 was performed except that the ultraviolet absorber of Example 1 was not added.

[Comparative Example 2]
The same procedure as in Example 1 was performed except that cesium carbonate was used instead of calcium acetate monohydrate.

  In addition, about the aromatic monohydroxy compound content of the said Example and comparative example, most was substantially phenol.

  As the results of Table-1 show, the molded article of the polycarbonate resin composition produced in Examples 1 to 3 is different from the one produced in Comparative Examples 1 and 2 in the difference in YI value before and after the metal halide lamp irradiation treatment. The absolute value of the haze value before and after the metal halide lamp irradiation treatment was small. That is, the molded article of the polycarbonate resin composition produced in Examples 1 to 3 was superior in weather resistance to those produced in Comparative Examples 1 and 2.

  The polycarbonate resin composition of the present invention is excellent in weather resistance, hue, heat resistance, moldability, and mechanical strength, such as injection molding fields such as electric / electronic parts and automotive parts, and extrusion fields such as films and sheets. It is possible to provide materials in a wide range of fields.

Claims (7)

A polycarbonate resin composition comprising a polycarbonate resin in which the proportion of structural units derived from a dihydroxy compound represented by the following formula (2) relative to structural units derived from all dihydroxy compounds is 20 mol% or more, and an ultraviolet absorber. And
The polycarbonate resin has a light transmittance of 65% or more at a wavelength of 350 nm of a molded body (thickness 3 mm) molded from the polycarbonate resin.
The polycarbonate resin includes a structural unit derived from an aliphatic dihydroxy compound,
Containing 0.05 parts by weight or more and 5 parts by weight or less of an ultraviolet absorber with respect to 100 parts by weight of the polycarbonate resin;
0.0001 part by weight or more and 1 part by weight or less of an antioxidant with respect to 100 parts by weight of the polycarbonate resin,
In addition, the catalyst contains at least one metal compound selected from the group consisting of lithium and a metal of Group 2 of the long-period periodic table, and the amount of the metal compound contained as the catalyst is a polycarbonate resin composition. A polycarbonate resin composition characterized in that the total amount of metals is 20 ppm by weight or less based on the total.

  The polycarbonate resin composition according to claim 1, wherein the polycarbonate resin has a light transmittance at 320 nm of a molded product (thickness 3 mm) molded from the polycarbonate resin of 30% or more. The polycarbonate resin contains a structural unit derived from a dihydroxy compound containing a dihydroxy compound represented by the formula (2) and a structural unit derived from a carbonic acid diester represented by the following formula (3). Or the polycarbonate resin composition of 2.

(In the above formula (3), A ¹ and A ² are each independently a substituted or unsubstituted aliphatic hydrocarbon group having 1 to 18 carbon atoms, or a substituted or unsubstituted aromatic hydrocarbon group. And A ¹ and A ² may be the same or different.) The catalyst is at least one metal compound selected from the group consisting of a lithium compound and a metal of Group 2 of the long-period periodic table, and the total amount of these metal compounds is the amount of metal per 1 mol of the dihydroxy compound used. The polycarbonate resin composition according to any one of claims 1 to 3 , which is 20 µmol or less. The polycarbonate resin composition according to claim 4 , wherein the catalyst is at least one metal compound selected from the group consisting of a magnesium compound and a calcium compound. The polycarbonate resin composition according to any one of claims 1 to 5 , wherein a total content of sodium, potassium and cesium in the polycarbonate resin is 1 ppm by weight or less as a metal amount. A polycarbonate resin molded article comprising the polycarbonate resin composition according to any one of claims 1 to 6 .