JP2014098094A - Polycarbonate resin composition and method for producing the same - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a polycarbonate resin suppressed in viscosity reduction during melting.SOLUTION: There is provided a polycarbonate resin composition which contains a compound (B) having three or more functional groups of at least one selected from the group consisting of carbodiimide, isocyanate, epoxy, silane, acid anhydride and oxazoline to a polycarbonate resin (A) having at least a structural unit derived from a specific dihydroxy compound and contains an aromatic monohydroxy compound.

Description

  The present invention relates to a polycarbonate resin composition comprising a plant-derived raw material and excellent in heat resistance, transparency, weather resistance, mechanical strength, and melt stability.

Polycarbonate resins generally contain bisphenols as monomer components and take advantage of transparency, heat resistance, mechanical strength, etc., so-called electrical and electronic parts, automotive parts, optical recording media, optical fields such as lenses, etc. Widely used as engineering plastic.
Conventional polycarbonate resins are manufactured using raw materials derived from petroleum resources. However, in recent years, there is a concern about the exhaustion of petroleum resources, and there is a need to provide polycarbonate resins using raw materials obtained from biomass resources such as plants. It has been demanded. In addition, since there is concern that global warming due to an increase and accumulation of carbon dioxide emissions will lead to climate change, polycarbonate resin made from carbon-neutral plant-derived monomers as raw materials even after disposal after use Development is required.

  Under such circumstances, a method of obtaining a polycarbonate resin by using isosorbide (ISB), which is a dihydroxy compound obtained from biomass resources, as a monomer component, and distilling off a by-product monohydroxy compound under reduced pressure by transesterification with a carbonic acid diester. Has been proposed. The polycarbonate resin obtained from ISB has been studied for optical applications utilizing excellent optical properties in addition to use as a molding material utilizing heat resistance (see, for example, Patent Documents 1 to 4).

International Publication No. 2004/111106 Pamphlet Japanese Patent Laid-Open No. 2006-232897 JP 2006-28441 A JP 2008-24919 A

  According to the study by the present inventors, a polycarbonate resin composed of a dihydroxy compound having an alcoholic hydroxy group such as ISB or an aliphatic dihydroxy compound causes a carbonate-bond decarboxylation reaction at a high temperature. It has been found that the thermal stability is lower than that of the resin, and the molecular weight and melt viscosity are greatly reduced during various molding processes and compounds performed by melting the resin. As the molecular weight decreases, the mechanical properties decrease, so it is necessary to increase the initial molecular weight. On the other hand, the resin temperature increases due to shear heat generation, etc. There is also a problem of coloring. In order to solve such problems, an object of the present invention is to provide a polycarbonate resin in which a decrease in viscosity at the time of melting is suppressed.

As a result of intensive studies to solve the above-mentioned problems, the present inventor, with respect to 100 parts by weight of a polycarbonate resin (A) containing at least a structural unit derived from a dihydroxy compound represented by the following structural formula (1), 0.05 to 5 parts by weight of a compound (B) having at least one functional group selected from the group consisting of carbodiimide, isocyanate, epoxy, silane, acid anhydride, and oxazoline in a molecule of 3 or more, and The present inventors have found that a polycarbonate resin composition containing 1000 ppm by weight or less of an aromatic monohydroxy compound exhibits excellent quality and has high melt stability, leading to the present invention.

That is, the gist of the present invention is as follows.
(1) It consists of carbodiimide, isocyanate, epoxy, silane, acid anhydride, and oxazoline with respect to 100 parts by weight of polycarbonate resin (A) containing at least a structural unit derived from a dihydroxy compound represented by the following structural formula (1). Containing 0.05 to 5 parts by weight of a compound (B) having three or more functional groups selected from the group in one molecule and containing 1000 ppm by weight or less of an aromatic monohydroxy compound. A polycarbonate resin composition.

(2) The polycarbonate resin composition as described in (1), wherein the increase amount of the aromatic monohydroxy compound after heating the polycarbonate resin composition at 260 ° C. for 60 minutes is 700 ppm by weight or less.
(3) The polycarbonate resin composition according to (1) or (2), wherein the polycarbonate resin has a glass transition temperature of 80 ° C. or higher and 180 ° C. or lower.
Please correct the red marker below.
(4) The melt viscosity of the polycarbonate resin at a measurement temperature of 250 ° C. and a shear rate of 91.2 sec ⁻¹ is 300 Pa · s to 3000 Pa · s, and any one of (1) to (3) The polycarbonate resin composition according to item.
(5) In any one of (1) to (4), the polycarbonate resin contains 30% by weight or more of a structural unit derived from the dihydroxy compound represented by the structural formula (1). The polycarbonate resin composition as described.
(6) The polycarbonate resin contains 5% by weight or more and 80% by weight or less of a structural unit derived from an aliphatic dihydroxy compound or an alicyclic dihydroxy compound. 2. The polycarbonate resin composition according to item 1.
(7) At least one phosphorous compound selected from the group consisting of phosphoric acid, phosphorous acid, hypophosphorous acid, polyphosphoric acid, phosphonic acid, phosphonic acid ester, acidic phosphoric acid ester, and aliphatic cyclic phosphorous acid ester The polycarbonate resin composition according to any one of (1) to (6), comprising:
(8) The polycarbonate resin composition according to (7), wherein the phosphorus compound is contained in an amount of 1 ppm by weight to 8 ppm by weight as the amount of phosphorus atoms.
(9) The polycarbonate according to any one of (1) to (8), wherein a total content of sodium, potassium and cesium in the polycarbonate resin is 1 ppm by weight or less as a metal amount. Resin composition.
(10) The method for producing a polycarbonate resin composition according to any one of (1) to (9), wherein the polycarbonate resin (A) and the compound (B) are mixed with a bent twin screw extruder. A method for producing a polycarbonate resin composition, characterized by using and kneading.
(11) The method for producing a polycarbonate resin composition according to (10), wherein a resin temperature at the exit of the extruder is 200 ° C. or higher and 280 ° C. or lower.
(12) In the said extruder, the volatilization rate of an aromatic monohydroxy compound is 20% or more, The manufacturing method of the polycarbonate resin composition as described in (10) or (11) characterized by the above-mentioned.

  Since the polycarbonate resin composition of the present invention is excellent in heat resistance, transparency, weather resistance, and mechanical strength, it can be provided as a material applicable to various injection molding fields and extrusion molding fields. Furthermore, since the decrease in viscosity under melting is small, it can be used without lowering the inherent physical properties even under molding processing conditions at higher temperatures.

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.
The polycarbonate resin composition of the present invention is composed of carbodiimide, isocyanate, epoxy, silane, acid with respect to 100 parts by weight of the polycarbonate resin (A) containing at least a structural unit derived from a dihydroxy compound represented by the following structural formula (1). Compound (B) having at least three functional groups selected from the group consisting of anhydrides and oxazolines in three molecules or more
Is a polycarbonate resin composition containing 0.1 to 0.05 parts by weight of an aromatic monohydroxy compound and 1000 ppm by weight or less.

<Polycarbonate resin (A)>
Hereinafter, the structure of the polycarbonate resin of the present invention and the method for producing the same will be described in detail.
<Raw material>
(Dihydroxy compound)
The polycarbonate resin of the present invention contains at least a structural unit derived from the dihydroxy compound represented by the structural formula (1) (hereinafter sometimes referred to as “the dihydroxy compound of the present invention”). Examples of the dihydroxy compound of the present invention include isosorbide (ISB), isomannide and isoidet which are in a stereoisomeric relationship. Among these dihydroxy compounds, isosorbide obtained by dehydration condensation of sorbitol produced from various starches that are abundant as plant-derived resources and are readily available is most preferable. These may be used individually by 1 type and may be used in combination of 2 or more type.

According to the required performance of the polycarbonate resin obtained, the dihydroxy compound of the present invention,
They may be used alone or in combination of two or more. The polycarbonate resin of the present invention preferably contains 30% by weight or more of the structure derived from the dihydroxy compound of the present invention from the viewpoints of heat resistance and optical properties. More preferably, it is 35 weight% or more, Most preferably, it is 40 weight% or more. Further, if the content is too large, the mechanical properties may be lowered. Therefore, the upper limit value is preferably 80% by weight or less, more preferably 75% by weight or less, and particularly preferably 70% by weight or less.
The dihydroxy compound of the present invention may contain a stabilizer such as a reducing agent, antioxidant, oxygen scavenger, light stabilizer, antacid, pH stabilizer or heat stabilizer. In particular, since the dihydroxy compound of the present invention is easily altered under acidic conditions, it is preferable to include a basic stabilizer.
Examples of the basic stabilizer include hydroxides, carbonates, phosphates, phosphites, hypophosphites of group 1 or group 2 metals in the long-period periodic table (Nomenclature of Inorganic Chemistry IUPAC Recommendations 2005). Acid salts, borates and fatty acid salts, tetramethylammonium hydroxide, tetraethylammonium hydroxide, tetrapropylammonium hydroxide, tetrabutylammonium hydroxide, trimethylethylammonium hydroxide, trimethylbenzylammonium hydroxide, trimethylphenylammonium hydroxide, Triethylmethylammonium hydroxide, triethylbenzylammonium hydroxide, triethylphenylammonium Basic ammonium compounds such as dimethyl hydroxide, tributylbenzylammonium hydroxide, tributylphenylammonium hydroxide, tetraphenylammonium hydroxide, benzyltriphenylammonium hydroxide, methyltriphenylammonium hydroxide and butyltriphenylammonium hydroxide, diethylamine, di Butylamine, triethylamine, morpholine, N-methylmorpholine, diethanolamine, pyrrolidine, piperidine, 3-amino-1-propanol, ethylenediamine, N-methyldiethanolamine, diethylethanolamine, 4-aminopyridine, 2-aminopyridine, N, N- Dimethyl-4-aminopyridine, 4-diethylaminopyridine, 2-hydroxypyri Amine compounds such as gin, 2-methoxypyridine, 4-methoxypyridine, 2-dimethylaminoimidazole, 2-methoxyimidazole, imidazole, 2-mercaptoimidazole, 2-methylimidazole and aminoquinoline, and di- (tert-butyl) ) Hindered amine compounds such as amine and 2,2,6,6-tetramethylpiperidine. Among the stabilizers, diethanolamine, tetramethylammonium hydroxide, imidazole or hindered amine compounds are preferable from the viewpoint of stabilizing effect.

The content of these basic stabilizers in the dihydroxy compound is not particularly limited. However, since the dihydroxy compound used in the present invention is unstable in an acidic state, the content of the dihydroxy compound of the present invention including the stabilizer is not limited. It is preferable to add a stabilizer so that the pH of the aqueous solution is 7 or more.
If the amount is too small, the effect of preventing the alteration of the dihydroxy compound of the present invention may not be obtained. If the amount is too large, the dihydroxy compound of the present invention may be modified. It is preferably 0.0001 to 1% by weight, more preferably 0.001 to 0.1% by weight.

  If an alkali metal compound is used as a raw material for the production of a polycarbonate resin while being included in the dihydroxy compound of the present invention as these basic stabilizers, the basic stabilizer itself becomes a polymerization catalyst, and it becomes difficult to control the polymerization rate or quality. Without causing deterioration of the resin hue. For this reason, about the thing which has a basic stabilizer among the dihydroxy compounds of this invention, it is preferable to remove a basic stabilizer by an ion exchange resin or distillation before using it as a raw material for production of polycarbonate resin.

On the other hand, when a basic organic compound such as an amine compound is used as a stabilizer, the effect as a polymerization catalyst and the influence on coloring are small, and therefore, it can be used in a polymerization reaction without removing the stabilizer by distillation or the like.
In addition, since the dihydroxy compound of the present invention is gradually oxidized by oxygen, in order to prevent decomposition by oxygen during storage or handling during manufacture, water should not be mixed and an oxygen scavenger is used. Or in a nitrogen atmosphere.

  The polycarbonate resin of the present invention may contain a structural unit derived from a dihydroxy compound other than the above-mentioned dihydroxy compound of the present invention (hereinafter sometimes referred to as “other dihydroxy compound”). Examples of the other dihydroxy compounds include, for example, linear aliphatic hydrocarbon dihydroxy compounds, linear branched aliphatic hydrocarbon dihydroxy compounds, alicyclic hydrocarbon dihydroxy compounds, aromatic bisphenols, and aliphatic heterocyclic structures. And dihydroxy compounds having an ether group bonded to an aromatic group in the main chain.

  Examples of the straight-chain aliphatic hydrocarbon dihydroxy compound include ethylene glycol, 1,3-propanediol, 1,2-propanediol, 1,4-butanediol, 1,3-butanediol, 1,2 -Butanediol, 1,5-heptanediol, 1,6-hexanediol, 1,10-decanediol, 1,12-dodecanediol and the like.

Examples of the dihydroxy compound of the linear branched aliphatic hydrocarbon include neopentyl glycol and hexylene glycol.
Examples of the alicyclic hydrocarbon dihydroxy compound include 1,2-cyclohexanediol, 1,2-cyclohexanedimethanol, 1,3-cyclohexanedimethanol, 1,4-cyclohexanedimethanol, and tricyclodecanedi. Methanol, pentacyclopentadecane dimethanol, 2,6-decalin dimethanol, 1,5-decalin dimethanol, 2,3-decalin dimethanol, 2,3-norbornane dimethanol, 2,5-norbornane dimethanol, 1, Examples thereof include dihydroxy compounds derived from terpene compounds such as 3-adamantane dimethanol and limonene.

Examples of the 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, 1,1-bis (4-hydroxyphenyl) -2-ethylhexane 1,1-bis (4-hydroxyphenyl) decane, 1,3-bis [2- (4-hydroxyphenyl) -2-propyl] benzene, 2,2-bis (4-hydroxyphenyl) octane, 2, 2-bis (4-hydroxyphenyl) nonane, 2,2-bis (4-hydroxyphenyl) decane, 3,3-bis (4-hydroxyphenyl) pentane, 1,1-bis (4-hydroxyphenyl) cyclohexane, Bis (4-hydroxyphenyl) sulfone, 2,4′-dihydroxydiphenylsulfone, bis (4-hydroxyphenyl) sulfide, 4,4′-dihydroxydiphenyl ether, 4,4′-dihydroxy-3,3′-dichlorodiphenyl ether, 4,4′-dihydroxy-2,5-diethoxydiphenyl ether, 9,9-bis (4-hydride) Xylphenyl) fluorene, 9,9-bis (4-hydroxy-3-methylphenyl) fluorene, 9,9-bis (4-hydroxy-3-ethylphenyl) fluorene, (4-hydroxy-3-n-propylphenyl) Fluorene, 9,9-bis (4-hydroxy-3-isopropylphenyl) fluorene, 9,9-bis (4-hydroxy-3-n-butylphenyl) fluorene, 9,9-bis (4-hydroxy-3- sec-butylphenyl) fluorene, 9,9-bis (4-hydroxy-3-tert-butylphenyl) fluorene, 9,9-bis (4-hydroxy-3-cyclohexylphenyl) fluorene, 9,9-bis (4 -Hydroxy-3-phenylphenyl) fluorene and the like.

  Examples of the dihydroxy compound having an aliphatic heterocyclic structure include spiroglycol represented by the following formula (12) and the following formula (13).

Examples of the oxyalkylene glycols include diethylene glycol, triethylene glycol, tetraethylene glycol, polyethylene glycol, and polypropylene glycol.
Examples of the dihydroxy compound having an ether group bonded to the aromatic group in the main chain include 2,2-bis [4- (2-hydroxyethoxy) phenyl] propane, 2,2-bis [4- ( 2-hydroxypropoxy) phenyl] propane, 1,3-bis (2-hydroxyethoxy) benzene, 4,4′-bis (2-hydroxyethoxy) biphenyl and bis [4- (2-hydroxyethoxy) phenyl] sulfone, 9,9-bis [4- (2-hydroxyethoxy) phenyl] fluorene, 9,9-bis [4- (2-hydroxypropoxy) phenyl] fluorene, 9,9-bis [4- (2-hydroxyethoxy) -3-methylphenyl] fluorene, 9,9-bis [4- (2-hydroxypropoxy) -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.

  These other dihydroxy compounds may be used alone or in combination with the specific dihydroxy compound depending on the required performance of the obtained polycarbonate resin, or may be used in combination with the specific dihydroxy compound after combining two or more kinds. Good. Among them, from the viewpoint of the color tone, weather resistance, and optical properties of the polycarbonate resin, a dihydroxy compound having no aromatic ring structure in the molecular structure, that is, a dihydroxy compound of an aliphatic hydrocarbon or a dihydroxy compound of an alicyclic hydrocarbon is preferable. These may be used in combination.

Among the above, the aliphatic hydrocarbon dihydroxy compounds are particularly those having 3 to 6 carbon atoms such as 1,3-propanediol, 1,4-butanediol, 1,5-heptanediol or 1,6-hexanediol. A straight-chain aliphatic hydrocarbon dihydroxy compound having hydroxy groups at both ends is preferred.
As the alicyclic hydrocarbon dihydroxy compound, 1,2-cyclohexanedimethanol, 1,3-cyclohexanedimethanol, 1,4-cyclohexanedimethanol or tricyclodecane dimethanol is preferable, and 1,2 cyclohexanedimethanol is more preferable. -Dihydroxy compounds having a cyclohexane structure such as cyclohexanedimethanol, 1,3-cyclohexanedimethanol or 1,4-cyclohexanedimethanol, and most preferred is 1,4-cyclohexanedimethanol.

By using these other dihydroxy compounds in combination with the specific dihydroxy compound, it is possible to obtain effects such as improvement in flexibility and mechanical properties of the polycarbonate resin and improvement in moldability. However, if the content of the structural unit derived from the other dihydroxy compound is too large, the mechanical properties or heat resistance may be lowered. Therefore, in the polycarbonate resin of the present invention, the other dihydroxy compound The proportion of the derived structural unit is preferably 80% by weight or less, more preferably 70% by weight or less, and particularly preferably 60% by weight or less. On the other hand, it is preferably 5% by weight or more, more preferably 10% by weight or more, and particularly preferably 15% by weight or more.
(Carbonated diester)
The polycarbonate resin of the present invention can be obtained by polycondensation by a transesterification reaction using a dihydroxy compound containing the above-mentioned specific dihydroxy compound and a carbonic acid diester as raw materials. As a carbonic acid diester used, what is normally represented by following formula (6) is mentioned. These carbonic acid diesters may be used alone or in combination of two or more.

In the formula (6), A ¹ and A ² are each 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. A preferable example of A ¹ and A ² is a substituted or unsubstituted aromatic hydrocarbon group, and a more preferable example is an unsubstituted aromatic hydrocarbon group.

Examples of the carbonic acid diester represented by the formula (6) include substituted diphenyl carbonates such as diphenyl carbonate (DPC) and ditolyl carbonate, dimethyl carbonate, diethyl carbonate, and di-t-butyl carbonate. Among them, preferred is diphenyl carbonate or substituted diphenyl carbonate, and particularly preferred is diphenyl carbonate.
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 of the present invention is produced by transesterifying the above-mentioned dihydroxy compound and carbonic acid diester. More specifically, it can be obtained by transesterification and removing by-product monohydroxy compounds and the like out of the system.
In the transesterification reaction, polycondensation is performed in the presence of a transesterification reaction 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 of the present invention may be used. ) Can greatly affect the reaction rate or the quality of the polycarbonate resin obtained by polycondensation.

  The catalyst used is not limited as long as it can satisfy the transparency, hue, heat resistance, weather resistance, and mechanical strength of the produced polycarbonate resin. For example, metal compounds of Group 1 or Group 2 (hereinafter simply referred to as “Group 1” or “Group 2”) in the long-period periodic table, as well as basic boron compounds, basic phosphorus compounds, and basic ammonium compounds And basic compounds such as amine compounds. Preferably, Group 1 metal compounds and / or Group 2 metal compounds are used.

  Examples of the Group 1 metal compound include sodium hydroxide, potassium hydroxide, lithium hydroxide, cesium hydroxide, sodium hydrogen carbonate, potassium hydrogen carbonate, lithium hydrogen carbonate, cesium hydrogen carbonate, sodium carbonate, potassium carbonate, and carbonic acid. Lithium, cesium carbonate, sodium acetate, potassium acetate, lithium acetate, cesium acetate, sodium stearate, potassium stearate, lithium stearate, cesium stearate, sodium borohydride, potassium borohydride, lithium borohydride, hydrogenated Cesium boron, sodium phenide boron, potassium phenide boron, lithium phenide boron, cesium phenide boron, sodium benzoate, potassium benzoate, lithium benzoate, cesium benzoate, hydrogen phosphate 2 Thorium, 2 potassium hydrogen phosphate, 2 lithium hydrogen phosphate, 2 cesium hydrogen phosphate, 2 sodium phenyl phosphate, 2 potassium phenyl phosphate, 2 lithium phenyl phosphate, 2 cesium phenyl phosphate, sodium, potassium, lithium, Examples include cesium alcoholate, phenolate, disodium salt of bisphenol A, dipotassium salt, dilithium salt, and dicesium salt. Among these, lithium compounds are preferable from the viewpoint of polymerization activity and the hue of the obtained polycarbonate resin.

  Examples of the Group 2 metal compound include calcium hydroxide, barium hydroxide, magnesium hydroxide, strontium hydroxide, calcium hydrogen carbonate, barium hydrogen carbonate, magnesium hydrogen carbonate, strontium hydrogen carbonate, calcium carbonate, barium carbonate, carbonic acid. Examples thereof include magnesium, strontium carbonate, calcium acetate, barium acetate, magnesium acetate, strontium acetate, calcium stearate, barium stearate, magnesium stearate, and strontium stearate. Among these, a magnesium compound, a calcium compound or a barium compound is preferable, and a magnesium compound and / or a calcium compound is more preferable, and a calcium compound is most preferable from the viewpoint of polymerization activity and the hue of the obtained polycarbonate resin.

In addition, a basic compound such as a basic boron compound, a basic phosphorus compound, a basic ammonium compound, and an amine compound can be used in combination with the above-mentioned Group 1 metal compound and / or Group 2 metal compound. However, it is particularly preferred to use only Group 1 metal compounds and / or Group 2 metal compounds.
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 Dorokishido and 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, and 4-methoxypyridine. 2-dimethylaminoimidazole, 2-methoxyimidazole, imidazole, 2-mercaptoimidazole, 2-methylimidazole, aminoquinoline, guanidine and the like.

The amount of the polymerization catalyst used is preferably 0.1 μmol to 300 μmol, more preferably 0.5 μmol to 100 μmol, per 1 mol of all dihydroxy compounds used in the polymerization. 1 μmol to 50 μmol is particularly preferable.
In particular, when using a compound containing at least one metal selected from the group consisting of Group 2 and lithium in the long-period periodic table, particularly when using a magnesium compound and / or a calcium compound, the amount of metal is The amount is preferably 0.1 μmol or more, more preferably 0.3 μmol or more, and particularly preferably 0.5 μmol or more per 1 mol of the dihydroxy compound. Moreover, as an upper limit, 20 micromol or less is preferable, More preferably, it is 10 micromol or less, More preferably, it is 5 micromol or less, Most preferably, it is 3 micromol or less.

  If the amount of the catalyst is too small, the polymerization rate is slowed down. Therefore, in order to obtain a polycarbonate resin having a desired molecular weight, the polymerization temperature must be increased accordingly. Therefore, there is a high possibility that the hue of the obtained polycarbonate resin is deteriorated, and the unreacted raw material volatilizes during the polymerization, and the molar ratio of the dihydroxy compound and the carbonic acid diester collapses, and the desired molecular weight may not be reached. There is sex. On the other hand, if the amount of the polymerization catalyst used is too large, undesirable side reactions may occur, and the resulting polycarbonate resin may be deteriorated in hue or colored during molding.

  However, if a large amount of sodium, potassium or cesium is included in the polycarbonate resin, the hue may be adversely affected. And these metals may mix not only from the catalyst to be used but from a raw material or a reaction apparatus. Regardless of the source, the total amount of these metal compounds in the polycarbonate resin is preferably 1 ppm by weight or less as the amount of metal. Furthermore, it is preferable that it is 0.5 weight ppm or less.

(Production method of polycarbonate resin)
The polycarbonate resin of the present invention can be obtained by polycondensing a dihydroxy compound containing a specific dihydroxy compound and a carbonic acid diester by a transesterification reaction.
The raw material dihydroxy compound and carbonic acid diester are preferably mixed uniformly before the transesterification reaction. 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, 100 ° 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 of the present invention, which is the raw material of the polycarbonate resin of the present invention, and the carbonic acid diester is performed at an oxygen concentration of 10 vol% or less, more preferably 0.0001 vol% to 10 vol%, and more preferably 0.0001 vol% to 5 vol. %, Particularly 0.0001 vol% to 1 vol%, is preferable from the viewpoint of preventing hue deterioration.

  In order to obtain the resin of the present invention, it is preferable to use a carbonic acid diester in a molar ratio of 0.90 to 1.20, more preferably 0.000 to all dihydroxy compounds including the specific dihydroxy compound used in the reaction. The molar ratio is 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 resin 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 of the present invention, the amount of residual carbonic acid diester in the obtained polycarbonate resin increases, resulting in problems of dirt and odor during molding. In some cases, it is not preferable.

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 a batch method, a continuous method, or a combination of a batch method and a continuous method, but a continuous method is preferred, in which a polycarbonate resin can be obtained with less heat history and excellent productivity.
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. Appropriate selection of the internal temperature and pressure in the reaction system is important from the viewpoint of controlling the polymerization rate and the quality of the polycarbonate resin obtained. 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. Or a polymer having a predetermined molecular weight or terminal group cannot be obtained, and as a result, the object of the present invention may not be achieved.

  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 condenser can be appropriately selected according to the monomer used, but the temperature of the refrigerant introduced into the reflux condenser is usually 45 to 180 ° C. at the inlet of the reflux condenser. Yes, preferably 80 to 150 ° C, particularly preferably 100 to 130 ° C. 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 while not impairing the hue of the final polycarbonate resin, it is important to select the kind and amount of the catalyst described above. The polycarbonate resin of the present invention is preferably produced by polymerizing in a plurality of stages using a catalyst and using a plurality of reactors, but the reason for carrying out the polymerization in a plurality of reactors is the reaction at the initial stage of the polymerization reaction. Since many monomers are contained in the liquid, it is important to suppress the volatilization of the monomers while maintaining the necessary polymerization rate. In the late stage of the polymerization reaction, by-products are generated in order to shift the equilibrium to the polymerization side. This is because it is important to sufficiently distill off the 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 number of reactors used in the method of the present invention may be at least two or more. However, from the viewpoint of production efficiency, the number of reactors is three or more, preferably 3 to 5, and particularly preferably four. It is. 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 first stage reaction is carried out at 130 to 250 ° C., preferably 150 to 240 ° C., more preferably 170 to 230 ° C., and preferably 110 to 110 kPa, as the maximum internal temperature of the polymerization reactor. Is carried out at a pressure of 5 to 70 kPa, more preferably 7 to 30 kPa (absolute pressure) for 0.1 to 10 hours, preferably 0.5 to 3 hours, while distilling off the generated monohydroxy compound out of the reaction system. Is done.

  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. The pressure is set to 200 Pa or less, and the maximum internal temperature is 210 to 270 ° C., preferably 220 to 250 ° C., usually 0.1 to 10 hours, preferably 1 to 6 hours, particularly preferably 0.5 to 3 hours.

In order to obtain a polycarbonate resin having a predetermined molecular weight, if the polymerization temperature is high and the polymerization time is too long, the color tone tends to deteriorate. In particular, in order to suppress the coloring and thermal deterioration of the polycarbonate resin and obtain a polycarbonate resin having a good hue, it is preferable that the maximum internal temperature in all reaction stages is less than 250 ° C, particularly 220 to 245 ° C. In order to suppress the decrease in the polymerization rate in the latter half of the polymerization reaction and minimize degradation due to thermal history, it is necessary to use a horizontal reactor with excellent plug flow and interface renewability at the final stage of polymerization. preferable.
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 of 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.
When using an extruder, the residual monomer is devolatilized under reduced pressure, and commonly known thermal stabilizers, neutralizers, UV absorbers, mold release agents, colorants, antistatic agents, lubricants, lubricants, plasticizers, A compatibilizer, a flame retardant, etc. can be added and kneaded.

  It is preferable to add a phosphorus compound to the polycarbonate resin of the present invention in order to deactivate the polymerization catalyst and further suppress coloring of the polycarbonate resin at high temperature. The phosphorus compound includes at least one selected from the group consisting of phosphoric acid, phosphorous acid, hypophosphorous acid, polyphosphoric acid, phosphonic acid, phosphonic acid ester, acidic phosphoric acid ester, and aliphatic cyclic phosphite ester. It is preferable to use it. In particular, phosphorous acid, phosphonic acid, and phosphonic acid ester are preferable.

  Examples of phosphonic acid include phosphonic acid (phosphorous acid), methylphosphonic acid, ethylphosphonic acid, vinylphosphonic acid, decylphosphonic acid, phenylphosphonic acid, benzylphosphonic acid, aminomethylphosphonic acid, methylenediphosphonic acid, 1-hydroxyethane- Examples include 1,1-diphosphonic acid, 4-methoxyphenylphosphonic acid, nitrilotris (methylenephosphonic acid), and propylphosphonic anhydride.

  Examples of phosphonic acid esters include dimethyl phosphonate, diethyl phosphonate, bis (2-ethylhexyl) phosphonate, dilauryl phosphonate, dioleyl phosphonate, diphenyl phosphonate, dibenzyl phosphonate, dimethyl methylphosphonate, diphenyl methylphosphonate, and ethylphosphonic acid. Diethyl, diethyl benzylphosphonate, dimethyl phenylphosphonate, diethyl phenylphosphonate, dipropyl phenylphosphonate, diethyl (methoxymethyl) phosphonate, diethyl vinylphosphonate, diethyl hydroxymethylphosphonate, dimethyl (2-hydroxyethyl) phosphonate, p-methylbenzylphosphonate diethyl, diethylphosphonoacetic acid, diethylphosphonoacetic acid ethyl, diethylphosphonoacetic acid tert-butyl, (Robenzyl) diethyl phosphonate, diethyl cyanophosphonate, diethyl cyanomethylphosphonate, diethyl 3,5-di-tert-butyl-4-hydroxybenzylphosphonate, diethylphosphonoacetaldehyde diethyl acetal, diethyl (methylthiomethyl) phosphonate Can be mentioned.

Acid phosphate esters include dimethyl phosphate, diethyl phosphate, divinyl phosphate, dipropyl phosphate, dibutyl phosphate, bis (butoxyethyl) phosphate, bis (2-ethylhexyl) phosphate, diisotridecyl phosphate, phosphate Examples include phosphoric acid diesters such as dioleyl, distearyl phosphate, diphenyl phosphate, and dibenzyl phosphate, or mixtures of diesters and monoesters, diethyl chlorophosphate, and zinc stearyl phosphate.
An aliphatic cyclic phosphite is defined as a phosphite compound that does not contain an aromatic group in a cyclic structure containing a phosphorus atom. For example, bis (decyl) pentaerythritol diphosphite, bis (tridecyl) pentaerythritol diphosphite, distearyl pentaerythritol diphosphite, bis (2,6-tert-butylphenyl) pentaerythritol diphosphite, bis (nonyl) Phenyl) pentaerythritol diphosphite, bis (2,4-di-tert-butylphenyl) pentaerythritol diphosphite, bis (2,6-di-tert-butyl-4-methylphenyl) pentaerythritol diphosphite, Examples thereof include a polymer type compound composed of a dihydroxy compound such as hydrogenated bisphenol A / pentaerythritol phosphite polymer and pentaerythritol diphosphite.

  If the addition amount of the phosphorus compound is too small, the effects of catalyst deactivation and coloring suppression are insufficient, and if it is too much, the polycarbonate resin is colored instead. Therefore, the addition amount is 1 ppm by weight as the amount of phosphorus atoms As mentioned above, it is preferable to set it as 8 weight ppm or less. Furthermore, 1.2 weight ppm or more and 7 weight ppm or less are preferable, and 1.5 weight ppm or more and 6 weight ppm or less are particularly preferable.

  Since the phosphorus compound is usually phosphorus trichloride as a starting material, unreacted substances or detached chlorine-containing components derived from hydrochloric acid may remain. The amount of chlorine atoms contained in the phosphorus compound is preferably 5% by weight or less. When the residual amount of chlorine atoms is large, there is a concern that the metal part of the production facility to which the phosphorus compound is added is corroded, the thermal stability of the polycarbonate resin is lowered, and the molecular weight reduction due to coloring or thermal deterioration is promoted.

  As described above, the phosphorus compound is preferably added to and kneaded with the polycarbonate resin using an extruder. In particular, it is most effective to supply the polycarbonate resin to the extruder in a molten state after polymerization and immediately add the phosphorus compound to the resin. Further, when the catalyst is deactivated and devolatilization is performed by a vacuum vent with an extruder, low molecular components can be efficiently devolatilized.

By using a hindered phenol compound in combination with the phosphorus compound, further improvement in the color tone of the polycarbonate resin can be expected. Specific examples of hindered phenol compounds include 2,6-di-tert-butylphenol, 2,4-di-tert-butylphenol, 2-tert-butyl-4-methoxyphenol, and 2-tert-butyl- 4,6-dimethylphenol, 2,6-di-tert-butyl-4-methylphenol, 2,6-di-tert-butyl-4-ethylphenol, 2,5-di-tert-butylhydroquinone, n- Octadecyl-3- (3 ′, 5′-di-tert-butyl-4′-
Hydroxyphenyl) propionate, 2-tert-butyl-6- (3′-tert-butyl-5′-methyl-2′-hydroxybenzyl) -4-methylphenyl acrylate, 2,2′-methylene-bis- (4 -Methyl-6-tert-butylphenol), 2,2'-methylene-bis- (6-cyclohexyl-4-methylphenol), 2,2'-ethylidene-bis- (2,4-di-tert-butylphenol) Tetrakis- [methylene-3- (3 ′, 5′-di-tert-butyl-4′-hydroxyphenyl) propionate] -methane, n-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, 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] and the like.

The blending amount of the hindered phenol compound is preferably 0.001 to 1 part by mass, more preferably 0.005 to 0.5 part by mass, based on 100 parts by mass of the polycarbonate resin. 01 parts by mass to 0.3 parts by mass are more preferable.
The polycarbonate resin can be blended with an antioxidant generally known for the purpose of preventing oxidation. Specifically, triphenyl phosphite, tris (nonylphenyl) phosphite, tris (2,4-di-tert-butylphenyl) phosphite, tridecyl phosphite, trioctyl phosphite, trioctadecyl phosphite, di Decyl monophenyl phosphite, dioctyl monophenyl phosphite, diisopropyl monophenyl phosphite, monobutyl diphenyl phosphite, monodecyl diphenyl phosphite, monooctyl diphenyl phosphite, 2,2-methylenebis (4,6-di-tert- Butylphenyl) octyl phosphite, tris (2,4-di-tert-butylphenyl) phosphite, tributyl phosphate, triethyl phosphate, trimethyl phosphate, triphenyl phosphate , Diphenyl monoorthoxenyl phosphate, dibutyl phosphate, dioctyl phosphate, diisopropyl phosphate, 4,4′-biphenylenediphosphinic acid tetrakis (2,4-di-tert-butylphenyl), pentaerythritol tetrakis (3-mercaptopropionate) , Pentaerythritol tetrakis (3-laurylthiopropionate), glycerol-3-stearylthiopropionate, N, N-hexamethylenebis (3,5-di-tert-butyl-4-hydroxy-hydrocinnamide) , 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} -2,4,8,10-tetraoxaspiro (5,5) undecane and the like. It is done.

These heat stabilizers may be used alone or in combination of two or more. The blending amount of these heat stabilizers is preferably 0.0001 parts by mass to 0.1 parts by mass, more preferably 0.0005 parts by mass to 0.08 parts by mass, when the polycarbonate resin is 100 parts by mass. More preferred is 0.001 to 0.05 parts by weight.
The melt kneading temperature in the extruder depends on the glass transition temperature and molecular weight of the polycarbonate resin, but is usually 200 to 300 ° C, preferably 210 to 280 ° C, and more preferably 220 to 270 ° C. When the melt kneading temperature is lower than 200 ° C., the melt viscosity of the polycarbonate resin is high, the load on the extruder is increased, and the productivity is lowered. When the temperature is higher than 300 ° C., the polycarbonate resin is severely deteriorated by heat, resulting in a decrease in mechanical strength due to a decrease in molecular weight, coloring, and gas generation.

  The molecular weight of the polycarbonate resin of 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 0.33 dL / g or more, The upper limit is more preferably 1.20 dL / g or less and 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 tube at a temperature of 20.0 ° C. ± 0.1 ° C., using methylene chloride as a solvent and precisely preparing a polycarbonate resin concentration of 0.6 g / dL.

The melt viscosity of the polycarbonate resin composition of the present invention is preferably 300 Pa · s or more and 3000 Pa · s or less. Furthermore, it is preferably 400 Pa · s or more and 2700 Pa · s or less, and particularly preferably 500 Pa · s or more and 2500 Pa · s or less. If the melt viscosity is lower than the above range, the polycarbonate resin becomes brittle and the material does not have sufficient mechanical properties. On the other hand, if the melt viscosity is higher than the above range, the fluidity is insufficient at the time of molding, and the appearance of the molded product is impaired or the dimensional accuracy is deteriorated. Further, there is a concern that the resin temperature rises due to shear heat generation, and the resin is colored or foamed. In the present specification, the melt viscosity indicates a melt viscosity at a measurement temperature of 250 ° C. and a shear rate of 91.2 s ⁻¹ using a capillary rheometer [manufactured by Toyo Seiki Co., Ltd.].

  The glass transition temperature of the polycarbonate resin composition of the present invention is preferably 80 ° C. or higher and 180 ° C. or lower. Furthermore, it is preferably 90 ° C. or higher and 160 ° C. or lower, and particularly preferably 95 ° C. or higher and 140 ° C. or lower. If the glass transition temperature is too low, the molded product may be deformed at high temperatures or high humidity, and heat resistance that can withstand use cannot be satisfied. On the other hand, if the glass transition temperature is excessively high, the temperature must be increased during the molding process, resulting in thermal degradation such as a decrease in molecular weight or coloring of the polycarbonate resin, or the appearance of the molded product is impaired due to gas generation. There is a fear. The glass transition temperature of the present invention is measured using DSC. Details of the measurement conditions are described in the Examples section.

In the polycondensation reaction, an aromatic monohydroxy compound is generated as a leaving component from the carbonic acid diester. When diphenyl carbonate is used as the carbonic acid diester, the aromatic monohydroxy compound produced is phenol. Similar to the carbonic acid diester, if a large amount of the aromatic monohydroxy compound remains in the polycarbonate resin, there may be a problem during molding. The residual amount of the aromatic monohydroxy compound contained in the polycarbonate resin composition of the present invention is 1000 ppm by weight or less. Further, it is preferably 700 ppm by weight or less, and particularly preferably 300 ppm by weight or less. Reduce the residual amount of aromatic monohydroxy compounds in the polycarbonate resin by using an appropriate amount of the above-mentioned phosphorus compound that is a catalyst deactivator, performing sufficient devolatilization treatment, and combining these. And generation | occurrence | production under a heating can be suppressed.

In addition, aromatic monohydroxy compounds are generated not only during polymerization, but also when the polycarbonate resin is heated and molded and processed, because the polymerization reaction and thermal decomposition progress, and thus are generated even under heating conditions after polymerization. It is necessary to suppress it. In the polycarbonate resin composition of the present invention, the aromatic monohydroxy compound generated by heating at 260 ° C. for 60 minutes is preferably 700 ppm by weight or less. Further, it is preferably 500 ppm by weight or less, particularly preferably 300 ppm by polymerization or less.
If the content of the aromatic monohydroxy compound in the resin and the amount of heat generation are large, the functional group of the compound (B) described later reacts with the aromatic monohydroxy compound, and the desired characteristics cannot be obtained. Sometimes.

<Compound (B)>
The polycarbonate resin composition of the present invention contains at least one functional group selected from the group consisting of carbodiimide, isocyanate, epoxy, silane, acid anhydride, and oxazoline.
The compound (B) which has 3 or more in a molecule | numerator is contained.
The compound (B) has the functional group capable of binding to the terminal hydroxyl group of the polycarbonate resin. In order to suppress the decrease in the molecular weight of the polycarbonate resin, which is the object of the present invention, it is only necessary to cause a reaction to increase the molecular weight by bonding the terminal hydroxyl groups of the polycarbonate resin with the compound (B) under melting. Therefore, the compound (B) needs to have two or more of the functional groups in one molecule. However, since the above functional group also reacts with moisture in the polycarbonate resin and the aromatic monohydroxy compound, in order to efficiently bind the polymer chains as in the present invention, there are three or more functional groups in one molecule. It is characterized by having.

  In order to contain three or more functional groups in one molecule, a polymer or oligomer obtained by copolymerizing the monomer having the functional group by polycondensation or vinyl polymerization can be used as the compound (B). If the molecular weight of the compound (B) is too large, the compatibility with the polycarbonate resin is deteriorated, so that the kneaded resin composition may become cloudy. From the viewpoint of compatibility, the molecular weight of the compound (B) is preferably low. Moreover, it is possible to improve the transparency of the kneaded resin composition by adjusting the comonomer and copolymer composition to be combined to facilitate compatibility with the polycarbonate resin or by adjusting the refractive index.

The compound (B) contains at least one functional group selected from the group consisting of carbodiimide, isocyanate, epoxy, silane, acid anhydride, and oxazoline as a functional group. Specifically, it can be synthesized by copolymerizing a vinyl monomer having the functional group with a vinyl polymerization resin such as polyethylene, polypropylene, polyvinyl alcohol, polymethyl methacrylate, and polystyrene. For example, the following monomers are used.
Isocyanate: Isocyanate group-containing (meth) acrylic acid ester such as 2-isocyanatoethyl methacrylate and isocyanate group-containing styrene epoxy: Epoxy group-containing (meth) acrylic acid ester such as glycidyl methacrylate and epoxy group-containing styrene silane: Vinyltri Alkoxysilane group-containing vinyl monomer acid anhydrides such as alkoxysilane, vinylalkyltrialkoxysilane, trialkoxysilylnorbornene, p-styryltrialkoxysilane, and 3-methacryloxyalkyltrialkoxysilane: carboxylic acid anhydrides such as maleic anhydride Oxazoline: Oxazoline group-containing vinyl monomers such as 2-vinyl-2-oxazoline and 2-isopropenyl-2-oxazoline

For carbodiimide compounds, for example, by using an organophosphorus compound or an organometallic compound as a catalyst and subjecting various polyisocyanates to a decarboxylation condensation reaction at a temperature of about 70 ° C. or more in a solvent-free or inert solvent. A synthesized product can be used. As the polycarbodiimide compound contained in the carbodiimide compound, those produced by various methods can be used. Basically, conventional polycarbodiimide production methods (for example, US Pat. No. 2,941,956, Japanese Patent Publication No. 47-33279, J. Org. Chem. 28, 2069-2075 (1963), Chemical Review.
1981, Vol. 8, no. 4, p. 619-621) can be used.

  Examples of the organic diisocyanate that is a synthetic raw material in the production of the polycarbodiimide compound include aromatic diisocyanates, aliphatic diisocyanates, alicyclic diisocyanates, and mixtures thereof. Specifically, 1,5-naphthalene diisocyanate, 4,4′-diphenylmethane diisocyanate, 4,4′-diphenyldimethylmethane diisocyanate, 1,3-phenylene diisocyanate, 1,4-phenylene diisocyanate, 2,4-tolylene diisocyanate, 2,4-tolylene diisocyanate and 2,4′-diphenylmethane diisocyanate Mixture of 6-tolylene diisocyanate, hexamethylene diisocyanate, cyclohexane-1,4-diisocyanate, xylylene diisocyanate, isophorone diisocyanate, dicyclohexyl Tan-4,4'-diisocyanate, can be mentioned methyl cyclohexane diisocyanate, tetramethylxylylene diisocyanate, 2,6-diisopropylphenyl isocyanate, 1,3,5-triisopropylbenzene 2,4-diisocyanate and the like.

  Preferred examples of the carbodiimide compound (B) of the present invention include 4,4′-dicyclohexylmethane carbodiimide (degree of polymerization = 3 to 20), tetramethylenexylylene carbodiimide (degree of polymerization = 3 to 20), N, N-dimethyl. Examples thereof include phenylcarbodiimide (degree of polymerization 3 to 20), N, N′-di-2,6-diisopropylphenylcarbodiimide (degree of polymerization = 3 to 20), and the like. These may be used individually by 1 type and may use 2 or more types together.

  In the polycarbonate resin composition of the present invention, the content of the compound (B) of the present invention is 0.05 to 5 parts by weight, preferably 0.1 to 3 parts by weight based on 100 parts by weight of the polycarbonate resin (A). Parts, more preferably 0.3 to 2 parts by weight. If content of a compound (B) is less than 0.1 weight part, the effect which suppresses the molecular weight fall under melting of polycarbonate resin will become inadequate. On the other hand, when there is too much content of a compound (B), transparency may fall or a gel-like foreign material may generate | occur | produce.

The compound (B) is preferably added to and kneaded with the polycarbonate resin using an extruder in the same manner as the above-described heat stabilizer and the like. When the aromatic monohydroxy compound and moisture in the polycarbonate resin are vacuum devolatilized by kneading and using a bent type twin screw extruder as the extruder to be used, the effect of suppressing the decrease in molecular weight under melting by the compound (B) is obtained. It becomes easy to express efficiently. When the compound (B) and the polycarbonate resin (A) are kneaded, the volatilization rate of the aromatic monohydroxy compound in the polycarbonate resin (A) is preferably 20% or more. Also,
If the resin temperature rises too much during kneading, the desired properties may not be obtained due to the thermal decomposition of the polycarbonate resin (A) or compound (B), so the resin temperature at the extruder outlet should be 280 ° C or lower. It is preferable that the temperature be 270 ° C. or lower, particularly 260 ° C. or lower. Further, the lower limit value is preferably 200 ° C. or higher, more preferably 210 ° C. or higher, and particularly preferably 220 ° C. or higher, due to restrictions on the melt viscosity of the resin and the power of the extruder. The resin temperature at the exit of the extruder can be adjusted by the amount of resin processed, the rotational speed of the screw, the temperature setting of the cylinder, the selection of the screw element, and the like.

The polycarbonate resin of the present invention can be formed into a molded product by a generally known method such as an injection molding method, an extrusion molding method, or a compression molding method. In order to make use of the excellent transparency of the polycarbonate resin of the present invention, it is preferable to keep the transparency of the resin after kneading as high as possible by adjusting the composition and molecular weight of the compound (B) as described above. The polycarbonate resin composition of the present invention preferably has a total light transmittance of 70% or more of a plate molded body having a thickness of 3 mm. More preferably, it is 75% or more, and particularly preferably 80% or more.

The polycarbonate resin of the present invention includes, for example, aromatic polycarbonate resin, aromatic polyester, aliphatic polyester, polyamide, polystyrene, polyolefin, acrylic, amorphous polyolefin, ABS, AS and other synthetic resins, polylactic acid, polybutylene succinate. It can also be used as a polymer alloy by kneading with one or more of biodegradable resins such as rubber and rubber.
According to the present invention, a polycarbonate resin composition excellent in hue, transparency, heat resistance, weather resistance, optical characteristics, and mechanical strength can be provided.

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 the following, the physical properties and characteristics of the polycarbonate resin were evaluated by the following methods.
(1) Measurement of reduced viscosity
A polycarbonate resin sample was dissolved in methylene chloride to prepare a polycarbonate resin solution having a concentration of 0.6 g / dL. Measured at a temperature of 20.0 ° C. ± 0.1 ° C. using an Ubbelohde type viscosity tube manufactured by Moriyu Rika Kogyo Co., Ltd., and the relative viscosity η _rel is obtained from the following equation from the solvent passage time t ₀ and the solution passage time t ,
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.

(2) Measurement of Glass Transition Temperature of Polycarbonate Resin Measurement was performed using a differential scanning calorimeter (DSC 6220 manufactured by SII Nano Technology). About 10 mg of a resin sample was sealed in an aluminum pan manufactured by the same company, and the temperature was raised from room temperature to 250 ° C. at a temperature rising rate of 20 ° C./min under a nitrogen stream of 50 mL / min. After maintaining the temperature for 3 minutes, it was cooled to 30 ° C. at a rate of 20 ° C./min. The temperature was maintained at 30 ° C. for 3 minutes, and the temperature was increased again to 200 ° C. at a rate of 20 ° C./min. From the DSC data obtained at the second temperature increase, a straight line obtained by extending the base line on the low temperature side to the high temperature side, and a tangent line drawn at a point where the slope of the step change portion of the glass transition becomes maximum The extrapolated glass transition start temperature, which is the temperature of the intersection point, was determined and used as the glass transition temperature.

(3) Measurement of metal concentration in polycarbonate resin About 0.5 g of polycarbonate resin sample is precisely weighed in a microwave decomposition vessel manufactured by PerkinElmer, and 2 mL of 97% sulfuric acid is added to make it sealed and microwave at 230 ° C. for 10 minutes. Heated. 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.

(4) Measurement of melt viscosity of polycarbonate resin Polycarbonate resin pellets were vacuum-dried at 90 ° C for 5 hours or more. Measurement was performed with a capillary rheometer [manufactured by Toyo Seiki Co., Ltd.] using the dried sample. An orifice having a measurement temperature of 250 ° C. and a die diameter of 1 mmφ × 10 mmL was used. The resin was put into a cylinder and preheated for 5 minutes, and then the melt viscosity was measured at a shear rate of 91.2 sec- ¹ . The melt viscosity 10 minutes after the start of measurement is defined as the initial melt viscosity, and the melt viscosity 30 minutes after the start of measurement is defined as the staying melt viscosity. The ratio of the staying melt viscosity to the initial melt viscosity was defined as the melt viscosity retention rate.

(5) Measurement of total light transmittance of plate molded body The pellet of the polycarbonate resin composition was dried at 90 ° C. for 10 hours in a nitrogen atmosphere. Next, the dried polycarbonate resin composition pellets are supplied to an injection molding machine (J75EII type, manufactured by Nippon Steel Co., Ltd.), and the final cylinder temperature is 240 ° C. and the molding cycle is 23 seconds. 60 mm long × 3 mm thick) was molded. Based on JIS K7105, total light transmittance was measured with a D65 light source using a haze meter (color / turbidity simultaneous measuring device COH400, manufactured by Nippon Denshoku Industries Co., Ltd.). The greater the total light transmittance, the better the transparency.

(6) Measurement of aromatic monohydroxy compound content Approximately 1 g of a polycarbonate resin sample is precisely weighed and dissolved in 5 mL of methylene chloride to obtain a solution, and then acetone is added so that the total amount becomes 25 mL and reprecipitation is performed. It was. Next, the treatment liquid was filtered through a 0.2 μm disk filter and quantified by liquid chromatography.

(7) Measurement of heat generation amount of aromatic monohydroxy compound The polycarbonate resin was vacuum-dried at 90 ° C. for 5 hours or more. About 5 g of the dried polycarbonate resin was placed in a glass test tube, the inside of the container was purged with nitrogen, and then sealed with nitrogen. The test tube was immersed in an oil bath heated to 260 ° C. so that the polycarbonate resin pellets in the test tube were below the oil liquid level, and taken out from the oil bath after 60 minutes. After cooling to near room temperature, the resin is taken out, the amount of monohydroxy compound in the polycarbonate resin is measured by the method of (6) above, the amount of monohydroxy compound before heat treatment is subtracted, and the amount increased by heating Asked.

The abbreviations and manufacturers of the compounds used in the following examples are as follows.
・ ISB: Isosorbide (Rocket Fleure)
CHDM: 1,4-cyclohexanedimethanol [manufactured by SK Chemical Co.]
・ DPC: Diphenyl carbonate [Mitsubishi Chemical Corporation]
・ Bis (2-ethylhexyl) phosphonate [manufactured by Johoku Chemical Industry Co., Ltd.]
・ Carbodilite LA-1 (functional group: carbodiimide compound) [manufactured by Nisshinbo Chemical Co., Ltd.]
・ ARUFON UG-4040 (functional group: epoxy) [manufactured by Toagosei Co., Ltd.]
EHPE 3150 (functional group: epoxy) [manufactured by Daicel Corporation]
・ JONCRYL ADR4368 (functional group: epoxy) [made by BASF]
Epocross RPS-1005 (functional group: oxazoline) [manufactured by Nippon Shokubai Co., Ltd.]
・ Diacarna 30 (functional group: acid anhydride) [Mitsubishi Chemical Corporation]
・ Linkron XVF600N (functional group: silane) [Mitsubishi Chemical Corporation]
・ Linkron XHE740N (functional group: silane) [Mitsubishi Chemical Corporation]
Epolite 1600 (1,6-hexanediol diglycidyl ether) [manufactured by Kyoeisha Chemical Co., Ltd.]
・ Tolylene diisocyanate [manufactured by Tokyo Chemical Industry Co., Ltd.]
・ Pyromellitic anhydride [manufactured by Tokyo Chemical Industry Co., Ltd.]
[Production example of polycarbonate resin]

  Polycarbonate resin was polymerized using a continuous polymerization facility comprising three vertical stirring reactors, one horizontal stirring reactor, and a twin screw extruder. ISB, CHDM, and DPC were melted in tanks, ISB 25.6 kg / hr, CHDM 25.3 kg / hr, DPC 75.5 kg / hr (mole ratio ISB / CHDM / DPC = 0.500 / 0) .500 / 1.005) was continuously fed to the first vertical stirring polymerization tank. At the same time, an aqueous solution of calcium acetate monohydrate as a catalyst was supplied to the first vertical stirring reactor so as to be 1.5 μmol with respect to 1 mol of all dihydroxy compounds. The liquid level was kept constant while controlling the opening degree of the valve provided in the transfer pipe at the bottom of the reactor so that the average residence time in the first vertical stirring reactor was 90 minutes. The reaction liquid discharged from the bottom of the reactor is successively successively supplied to the second vertical stirring reactor, the third vertical stirring reactor, and the fourth horizontal stirring reactor [2-axis glasses blade manufactured by Hitachi Plant Technologies, Ltd.]. Continuously supplied. The first vertical stirring reactor and the second vertical stirring reactor were equipped with a reflux condenser, and the distillation of unreacted dihydroxy compound and DPC was suppressed by adjusting the reflux ratio.

  The reaction temperature, internal pressure, and residence time of each reactor are as follows. First vertical reactor: 190 ° C., 25 kPa, 90 minutes, second vertical reactor: 195 ° C., 10 kPa, 45 minutes, third vertical reactor : 210 ° C., 3 kPa, 45 minutes, fourth horizontal reactor: 225 ° C., 0.5 kPa, 90 minutes. The operation was performed while finely adjusting the internal pressure of the fourth horizontal reactor so that the reduced viscosity of the obtained polycarbonate resin was 0.61 to 0.64.

  The polycarbonate resin was extracted from the fourth horizontal stirring reactor at an amount of 60 kg / hr, and then the resin was supplied in a molten state to a twin-screw extruder [TEX30α manufactured by Nippon Steel Works]. The extruder had three vacuum vents, and the remaining low molecular components in the resin were removed by devolatilization. Master pellets coated with bis (2-ethylhexyl) phosphonate are supplied from the front side of the first vent of the extruder, and bis (2-ethylhexyl) phosphonate is 25 ppm by weight (as an amount of phosphorus atoms) with respect to the polycarbonate resin. 2.5 ppm by weight) was added. Before the second vent, water was added in an amount of 2000 ppm by weight with respect to the resin, and water injection devolatilization was performed. The extruder was set to a cylinder temperature of 220 ° C. and a screw rotation speed of 230 rpm.

  After the polycarbonate resin that has passed through the extruder is continuously melted and filtered through the filter, the polycarbonate resin is discharged from the die into strands, cooled with water, solidified, pelletized with a rotary cutter, and ISB / CHDM = 50 / 50 mol% of polycarbonate resin (A) was obtained. The polycarbonate resin (A) obtained had a melt viscosity of 1040 Pa · s and a glass transition temperature of 100 ° C. The content of the aromatic monohydroxy compound in the resin was 430 ppm by weight, and the total content of sodium, potassium and cesium was 0.1 ppm by weight.

[Example 1]
2 parts by weight of carbodilite LA-1 as compound (B) is added to 100 parts by weight of the polycarbonate resin (A) pellets, blended uniformly, and has a vent port. Were kneaded using. The resin temperature at the exit of the extruder was 254 ° C. The devolatilization rate of the aromatic monohydroxy compound in the extruder was 48%, and the heat generation amount was 119 ppm by weight. Using the pellets obtained by kneading, the total light transmittance and the melt viscosity retention were measured by the methods described above. The total light transmittance was 58.7%, which was a slightly low value. The melt viscosity retention was 83%, which was a good value. The results are summarized in Table 1.

[Example 2]
In Example 1, 1 part by weight of carbodilite LA-1 was used. The total light transmittance was 74.0%, which is an improvement over Example 1. The melt viscosity retention was 79%, which was slightly lower than that of Example 1, but showed a good value.
[Example 3]
In Example 1, 0.5 part by weight of carbodilite LA-1 was used. The total light transmittance was 82.6%, which was improved over those of Example 1 and Example 2. The melt viscosity retention was 76%, which was a good value although it was slightly lower than that of Example 1 or Example 2.

[Example 4]
In Example 2, kneading was performed by increasing the screw rotation speed of the extruder. The resin temperature at the exit of the extruder was 283 ° C. The total light transmittance was 78.2%, which was slightly improved from Example 2. However, the melt viscosity retention was 75%, which was slightly lower than Example 2.
[Example 5]
In Example 1, 1 part by weight of ARUFON UG-4040 was used instead of Carbodilite LA-1. The melt viscosity retention was 81%, which was a good value.

[Example 6]
In Example 1, 1 part by weight of EHPE 3150 was used instead of carbodilite LA-1. The melt viscosity retention was 83%, which was a good value. Further, the total light transmittance was 87.0%, and the transparency was excellent.
[Example 7]
In Example 1, 1 part by weight of JONCRYL ADR4368 was used in place of Carbodilite LA-1. The melt viscosity retention was 79%, which was a good value. Further, the total light transmittance was 89.6%, and the transparency was excellent.

[Example 8]
In Example 1, 1 part by weight of Epocross RPS-1005 was used instead of Carbodilite LA-1. The melt viscosity retention was 80%, which was a good value.
[Example 9]
In Example 1, 1 part by weight of Diacarna 30 was used instead of Carbodilite LA-1. The melt viscosity retention was 83%, which was a good value.

[Example 10]
In Example 1, 1 part by weight of Linkron XHE740N was used instead of Carbodilite LA-1. The melt viscosity retention was 78%, which was a good value.
[Example 11]
In Example 1, 1 part by weight of Linklon XVF600N was used instead of Carbodilite LA-1. The melt viscosity retention was 81%, which was a good value. Further, the total light transmittance was 85.8%, and the transparency was excellent.

[Comparative Example 1]
In Example 1, the compound (B) was not used. The melt viscosity retention was 70%, and the molecular weight decrease under melting was large.
[Comparative Example 2]
In the production example of polycarbonate resin, vacuum devolatilization with an extruder was not performed. Moreover, bis (2-ethylhexyl) phosphonate was not added with an extruder. The content of the aromatic monohydroxy compound in the obtained polycarbonate resin was 1160 ppm by weight. 1 part by weight of carbodilite LA-1 as compound (B) was added to 100 parts by weight of the polycarbonate resin pellets, blended uniformly, and kneaded using a vent type twin screw extruder. At this time, the vent of the extruder was not used. The resin temperature at the exit of the extruder was 251 ° C. The amount of heat generation of the monohydroxy compound in the pellets after kneading was 1120 ppm by weight, and the amount of heat generation was also very high at 905 ppm by weight. The melt viscosity retention rate was 73%, which was a low value compared to Example 2 in which the same amount of carbodilite LA-1 was added.

[Comparative Example 3]
In Example 1, 1 part by weight of bifunctional epolite 1600 was used as the compound (B). The melt viscosity retention rate was 72%, which was lower than in each example.
[Comparative Example 4]
In Example 1, 1 part by weight of bifunctional tolylene diisocyanate was used as the compound (B). The melt viscosity retention was 73%, which was lower than in each example.

[Comparative Example 5]
In Example 1, 1 part by weight of bifunctional pyromellitic anhydride was used as the compound (B). The melt viscosity retention rate was 72%, which was lower than in each example.

  According to the present invention, a polycarbonate resin composition excellent in hue, transparency, heat resistance, weather resistance, optical characteristics, and mechanical strength can be provided.

Claims (12)

Selected from the group consisting of carbodiimide, isocyanate, epoxy, silane, acid anhydride, and oxazoline with respect to 100 parts by weight of polycarbonate resin (A) containing at least a structural unit derived from a dihydroxy compound represented by the following structural formula (1) Containing 0.05 to 5 parts by weight of the compound (B) having 3 or more of at least one functional group in one molecule and 1000 ppm by weight or less of an aromatic monohydroxy compound Polycarbonate resin composition.

  2. The polycarbonate resin composition according to claim 1, wherein the amount of the aromatic monohydroxy compound after heating the polycarbonate resin composition at 260 ° C. for 60 minutes is 700 ppm by weight or less.   The polycarbonate resin composition according to claim 1, wherein the polycarbonate resin has a glass transition temperature of 80 ° C. or higher and 180 ° C. or lower. 4. The polycarbonate according to claim ¹ , wherein the polycarbonate resin has a melt viscosity of 300 Pa · s or more and 3000 Pa · s or less at a measurement temperature of 250 ° C. and a shear rate of 91.2 sec ⁻¹ . Resin composition.   The polycarbonate resin composition according to any one of claims 1 to 4, wherein the polycarbonate resin contains 30% by weight or more of a structural unit derived from the dihydroxy compound represented by the structural formula (1). object.   The polycarbonate resin contains 5 to 80% by weight of a structural unit derived from an aliphatic dihydroxy compound or an alicyclic dihydroxy compound. Polycarbonate resin composition.   Contains at least one phosphorous compound selected from the group consisting of phosphoric acid, phosphorous acid, hypophosphorous acid, polyphosphoric acid, phosphonic acid, phosphonic acid ester, acidic phosphoric acid ester, and aliphatic cyclic phosphorous acid ester The polycarbonate resin composition according to any one of claims 1 to 6, wherein:   The polycarbonate resin composition according to claim 7, wherein the phosphorus compound is contained in an amount of 1 ppm by weight to 8 ppm by weight as the amount of phosphorus atoms.   The polycarbonate resin composition according to any one of claims 1 to 8, wherein the total content of sodium, potassium and cesium in the polycarbonate resin is 1 ppm by weight or less as a metal amount.   It is a manufacturing method of the polycarbonate resin composition of any one of Claims 1 thru | or 9, Comprising: The said polycarbonate resin (A) and the said compound (B) are knead | mixed using a vent type twin-screw extruder. A process for producing a polycarbonate resin composition characterized by the above.   11. The method for producing a polycarbonate resin composition according to claim 10, wherein a resin temperature at an exit of the extruder is 200 ° C. or higher and 280 ° C. or lower.   The method for producing a polycarbonate resin composition according to claim 10 or 11, wherein, in the extruder, the devolatilization rate of the aromatic monohydroxy compound is 20% or more.