JP3318917B2 - Copolycarbonate resin composition for optics - Google Patents

Description

DETAILED DESCRIPTION OF THE INVENTION

[0001]

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an optical copolycarbonate resin composition, and more particularly, to an optical disc,
The present invention relates to an optical copolycarbonate resin composition suitable for producing optical molded articles such as lenses and prisms.

[0002]

2. Description of the Related Art Polycarbonate is widely used because it has excellent mechanical properties such as impact resistance, and also has excellent heat resistance and transparency.

[0003] A generally known polycarbonate is produced using bisphenol A as a dihydroxy component, and has a linear molecular structure having a bisphenol A skeleton.

However, polycarbonate having such a linear molecular structure may be inferior in melt elasticity and melt strength at the time of melt molding, and it is desired to improve molding properties such as melt elasticity and melt strength. It is rare. As a method of improving such molding characteristics, a method of copolymerizing a polyfunctional compound to branch the polycarbonate is generally known (Japanese Patent Application Laid-Open No. 4-89824).

[0005] In the case of manufacturing optical molded products such as optical disks and lenses using polycarbonate, the molding temperature is reduced to reduce optical distortion and obtain a high degree of transfer from a mold.
It must be set at a high temperature of 300-400 ° C. In particular, in the production of optical disks, there is a tendency to shorten the molding cycle in order to increase production. Under these molding conditions, polycarbonate is exposed to high temperatures, and a sufficient cooling effect cannot be obtained due to the effect of the cycle shortening, and the so-called "nose dripping" often occurs when the molten polycarbonate drips from the tip of the heating cylinder of the molding machine. In addition, a problem such as so-called "stringing", which is a phenomenon in which the polycarbonate melted from the tip of the heating cylinder of the molding machine becomes a thread and extends to the sprue of the molded product, is likely to occur. These inconveniences not only severely limit molding conditions, but also cause a reduction in production efficiency.

Accordingly, an object of the present invention is to provide an optical polycarbonate resin composition capable of stably obtaining an optical molded product excellent in characteristics such as optical distortion and pit transferability under a wide range of molding conditions. I do.

[0007]

Means for Solving the Problems As a result of repeated studies on molding materials for optical products using polycarbonate, the present inventors have found that a specific structural unit is contained in a specific ratio and a molecular weight in a narrow specific range is reduced. By using a copolycarbonate having a resin composition containing an ester of an aliphatic carboxylic acid and a polyhydric alcohol, it has been found that an optical molded product having excellent properties can be obtained stably under a wide range of molding conditions, and the present invention Reached.

That is, the present invention relates to (A) a copolycarbonate obtained by copolymerizing at least two aromatic dihydroxy compounds and a compound capable of introducing a carbonic acid bond, As a component unit derived from a dihydroxy compound, the following formula [I]:

[0009]

Embedded image (In the formula, X is ^{- (R 3 -) C (} -R 4) -, - C
^{(= R 5) -, -} O -, - S -, - SO- or -SO
₂ --wherein R ³ and R ⁴ are a linear, branched or cyclic monovalent hydrocarbon group having 1 to 15 carbon atoms which may be substituted with a hydrogen atom or halogen, and R ⁵ is Is a linear, branched or cyclic divalent hydrocarbon group having 1 to 15 carbon atoms which may be substituted with halogen, and R ¹ and R ² may be the same or different A straight-chain, branched or cyclic hydrocarbon group having 1 to 10 carbon atoms which may be substituted with a halogen, or a halogen atom, m and n each represent the number of substituents, and each independently represents 0 A structural unit represented by the following formula [II]:

[0010]

Embedded image (In the above formula, Y is-(R3 ^' -) C (-R4 ^' )-, -C
(= R5 ^' )-, -O-, -S-, -SO- or -SO
₂ --wherein R ^{3 ′} and R ^{4 ′} are a hydrogen atom or a linear, branched or cyclic monovalent hydrocarbon group having 1 to 15 carbon atoms which may be substituted by a halogen atom; ^{5 ′} is a linear, branched or cyclic divalent hydrocarbon group having 1 to 15 carbon atoms which may be substituted with halogen, and R ⁷ and R ⁸ may be the same or different. Each may be a linear, branched or cyclic hydrocarbon group having 1 to 10 carbon atoms which may be substituted with a halogen, or a halogen atom, p and q represent the number of substituents, and p is Is an integer of 0 to 4, and q is an integer of 0 to 3)
And in shown a structural unit, wherein with respect to the structural units to 1 mol represented by [I], the structural unit 8 × 10 ^-5 of the formula [II]
(2) 100 parts by weight of a copolycarbonate having a viscosity average molecular weight of 12,000 to 18,000, and (B) an ester of an aliphatic carboxylic acid and a polyhydric alcohol in an amount of from 0.01 to 1.5 × 10 ^-3 mol. Provided is an optical copolycarbonate resin composition comprising 0.1 to 0.1 parts by weight.

The copolycarbonate (A) used in the present invention will be described. The copolycarbonate includes, as a structural unit derived from an aromatic dihydroxy compound, a structural unit represented by the above formula [I] and a structural unit represented by the above formula [II]
And a structural unit represented by

Among such aromatic dihydroxy compounds, examples of the aromatic dihydroxy compound for introducing the structural unit represented by the above formula [I] include the following formula [III]:

[0013]

Embedded image (In the above formula, X, R ¹ , R ² , m and n have the same meanings as described above). Here, as the monovalent hydrocarbon group, a linear, branched or cyclic alkyl group, alkenyl group, aryl group (for example, phenyl group), alkaryl group (for example, toluyl group), aralkyl group (for example, benzyl group) Group) and the like. Preferred examples of the monovalent hydrocarbon group include an alkyl group and an aryl group having 1 to 6 carbon atoms. Also,
Examples of the divalent hydrocarbon group include divalent groups in which these groups further have a free valence. Such compounds specifically include the following aromatic dihydroxy compounds: bis (4-hydroxyphenyl) methane, 1,1-bis (4-hydroxyphenyl) ethane, 2,2-bis (4-hydroxyphenyl) propane (ie, bisphenol A), 2,2-bis (4-hydroxyphenyl) butane, 2,2-bis (4-hydroxyphenyl) octane, bis (4-hydroxyphenyl) phenylmethane,
2,2-bis (4-hydroxy-3-methylphenyl) propane, 1,1-bis (4-hydroxy-3-t-butylphenyl) propane, 2,2-bis (4-hydroxy-3-bromophenyl) )
Bis (hydroxyaryl) alkanes such as propane and 2,2-bis (4-hydroxy-3,5-dimethylphenyl) propane; 1,1-bis (4-hydroxyphenyl) cyclopentane, 1,1-bis ( Bis (hydroxyaryl) cycloalkanes such as 4-hydroxyphenyl) cyclohexane; dihydroxyaryl ethers such as 4,4′-dihydroxydiphenyl ether and 4,4′-dihydroxy-3,3′-dimethylphenyl ether; 4,4 Dihydroxydiaryl sulfides such as' -dihydroxydiphenyl sulfide and 4,4'-dihydroxy-3,3'-dimethyldiphenyl sulfide; 4,4'-dihydroxydiphenyl sulphoxide, 4,4'-dihydroxy-3,3'-dimethyl Dihydroxydiarylsulfoxides such as diphenylsulfoxide; 4,4′-dihydroxydiphenylsulfone, 4,4′-di Such as dihydroxy diaryl sulfones such as Dorokishi 3,3'-dimethyl diphenyl sulfone.

Of these, 2,2-bis (4-hydroxyphenyl) propane is particularly preferred.

Next, as the aromatic dihydroxy compound for introducing the structural unit represented by the above formula [II], for example, a general formula [IV]:

[0016]

Embedded image (In the above formula, Y, R ⁷ , R ⁸ , p and q have the same meanings as described above, and R ⁶ is a hydrogen atom, a linear or branched C 1-20 carbon atom which may be substituted by halogen. Which is a cyclic hydrocarbon group or a halogen atom). Such compounds specifically include the following aromatic dihydroxy compounds: 2- (4-hydroxyphenyl) -2- (3'-carboxy-4'-hydroxyphenyl) propane, 2- ( 4-hydroxyphenyl) -2- (3'-methoxycarbonyl-4'-hydroxyphenyl) propane, 2- (4-hydroxyphenyl) -2- (3'-ethoxycarbonyl-4'-hydroxyphenyl) propane, 2 -(4-hydroxyphenyl) -2- (3'-butoxycarbonyl-4'-hydroxyphenyl) propane,
2- (4-hydroxyphenyl) -2- (3'-phenoxycarbonyl-4'-hydroxyphenyl) propane, 2- (4-hydroxyphenyl) -2- (3'-phenoxycarbonyl-4'-hydroxyphenyl) Methane, 2- (4-hydroxyphenyl)
-2- (3'-phenoxycarbonyl-4'-hydroxyphenyl) ethane, 2- (4-hydroxyphenyl) -2- (3'-phenoxycarbonyl-4'-hydroxyphenyl) octane,
1- (4-hydroxyphenyl) -1- (3′-phenoxycarbonyl-4′-hydroxyphenyl) cyclopentane, 4-hydroxyphenyl-3′-phenoxycarbonyl-4′-hydroxyphenyl ether, 4-hydroxy Phenyl-3'-phenoxycarbonyl-4'-hydroxyphenylsulfide, 4-
Hydroxyphenyl-3'-phenoxycarbonyl-4'-hydroxyphenylsulfoxide, 4-hydroxyphenyl-
3'-phenoxycarbonyl-4'-hydroxyphenylsulfone and the like.

Of these, 2- (4-hydroxyphenyl) -2- (3'-carboxy-4'-hydroxyphenyl) propane and 2- (4-hydroxyphenyl) -2- (3'-phenoxy) Carbonyl-4′-hydroxyphenyl) propane is preferred.

Such a compound can be prepared by using a desired aromatic dihydroxy compound by Kolbe-Schmidt.
mitt)
Alternatively, it can be easily synthesized by further esterification.

In the copolycarbonate (A) used in the present invention, the structural unit represented by the formula [II] is contained in an amount of 8 × 10 ^{−5 to} 1.5 × with respect to 1 mol of the structural unit represented by the formula [I].
In a ratio of 10 ^-3 mol, preferably 1.0 × 10 ^{-4 to} 1.0 × 10 ^-3
It is contained in a molar ratio. Below the lower limit of the above range, the melting property is reduced, it is difficult to mold an optical disc under a wide range of conditions, and above the upper limit of the above range, the melt viscosity becomes higher, when molding an optical disc, Optical distortion increases.

The (A) copolycarbonate used in the present invention contains a carbonic acid bond, and such a carbonic acid bond can be introduced using, for example, phosgene, carbonic acid diester, or the like. Specific examples of such carbonate diesters include the following compounds: diphenyl carbonate, ditolyl carbonate, bis (chlorophenyl) carbonate, m-cresyl carbonate, dinaphthyl carbonate, bis (diphenyl) carbonate, Diethyl carbonate, dimethyl carbonate, dibutyl carbonate, dicyclohexyl carbonate and the like. Of these, diphenyl carbonate is particularly preferred.

The (A) copolycarbonate used in the present invention may contain a structural unit derived from a dicarboxylic acid or a dicarboxylic acid ester in addition to the structural units described above. Such dicarboxylic acids or dicarboxylic esters include, for example, the following compounds: terephthalic acid, isophthalic acid, sebacic acid, decandioic acid, dodecandioic acid, diphenyl sebacate, diphenyl terephthalate, diphenyl isophthalate , Diphenyl decandioate, diphenyl dodecandioate and the like. When such a dicarboxylic acid or dicarboxylic acid ester is used in combination with a carbonic acid diester, a polyester polycarbonate is obtained. In the present invention, the above dicarboxylic acid or dicarboxylic acid ester can be contained in an amount of 50 mol or less, preferably 30 mol or less based on 100 mol of the carbonic acid diester.

The copolycarbonate (A) used in the present invention is an intrinsic viscosity number [η] measured in methylene chloride (0.5 g / dl) at 20 ° C. using an Ubbelohde viscometer.
From the formula:

[0023]

The viscosity average molecular weight (M) calculated by [η] = 1.23 × 10 ⁻⁴ × M ^0.83 is 12,000 to 18,0
It is characterized by being 00. If the viscosity average molecular weight is less than 12,000, the mechanical strength decreases, and if it is more than 18,000, inconveniences such as optical distortion and poor moldability occur.

The copolycarbonate (A) used in the present invention can be prepared, for example, using the above-mentioned aromatic dihydroxy compound represented by the general formula [III], the aromatic dihydroxy compound represented by the general formula [IV], and phosgene. It can be produced by an interfacial polycondensation method. However, it is preferable to manufacture by the following manufacturing method.

That is, the following formula [III]:

[0026]

Embedded image (Wherein X, R ¹ , R ² , m and n are as defined above), an aromatic dihydroxy compound represented by the following formula [IV]:

[0027]

Embedded image (Wherein, Y, R ⁶ , R ⁷ , R ⁸ , p and q are as defined above),
And the carbonic acid diester are melt-polycondensed in the presence of (a) a catalyst selected from alkali metal compounds and alkaline earth metal compounds.

As the aromatic dihydroxy compound represented by the general formula [III] and the aromatic dihydroxy compound represented by the general formula [IV], the compounds specifically described above can be preferably used.

The aromatic dihydroxy compound represented by the general formula [IV] is used in an amount of 8 × 10 ^{−5 to} 1.5 × 10 ⁻³ mol per 1 mol of the aromatic dihydroxy compound represented by the general formula [III]. It is preferably used at a ratio of 1.0 × 10 ^{−4 to} 1.0 × 10 ⁻³ mol.

As the carbonic acid diester, the compounds already specifically described above can be preferably used. Of these, diphenyl carbonate is preferred.

In this production method, the above-mentioned carbonic acid diester is used in an amount of 1.0 to 1.30 mol, preferably 1.0 mol, per 1 mol of the total of the aromatic dihydroxy compounds [III] and [IV]. It is preferably used in an amount of from 01 to 1.20 mol, more preferably from 1.01 to 1.10 mol.

In this production method, the above-mentioned dicarboxylic acid or dicarboxylic acid ester can be used in an amount of 50 mol or less, preferably 30 mol or less, based on 100 mol of the carbonic acid diester.

In this production method, the above compounds are melt-polycondensed in the presence of (a) a catalyst selected from an alkali metal compound and an alkaline earth metal compound.

Examples of the alkali metal compound or alkaline earth metal compound used as a catalyst include organic acid salts, inorganic acid salts, oxides, hydroxides, and the like of alkali metals or alkaline earth metals. Preferred are hydrides and alcoholates.

More specifically, such alkali metal compounds include sodium hydroxide, potassium hydroxide,
Lithium hydroxide, sodium bicarbonate, potassium bicarbonate, lithium bicarbonate, sodium carbonate, potassium carbonate, lithium carbonate, sodium acetate, potassium acetate, lithium acetate, sodium stearate, potassium stearate, lithium stearate, sodium borohydride , Lithium borohydride, sodium borohydride, sodium benzoate, potassium benzoate, lithium benzoate, disodium hydrogen phosphate, dipotassium hydrogen phosphate, dilithium hydrogen phosphate, disodium salt of bisphenol A, dipotassium Salts, dilithium salts, phenol sodium salts, potassium salts, lithium salts and the like are used.

Specific examples of the alkaline earth metal compound include calcium hydroxide, barium hydroxide, magnesium hydroxide, strontium hydroxide, calcium hydrogen carbonate, barium hydrogen carbonate, magnesium hydrogen carbonate, strontium hydrogen carbonate, and carbon dioxide. Calcium, barium carbonate,
Magnesium carbonate, strontium carbonate, calcium acetate, barium acetate, magnesium acetate, strontium acetate, calcium stearate, barium stearate, magnesium stearate, strontium stearate and the like are used.

These compounds can be used alone or in combination.

The catalyst (a) selected from the alkali metal compound and the alkaline earth metal compound (a) has a total (total amount) of the aromatic dihydroxy compounds [III] and [IV] of 1
1 × 10 ⁻⁸ to 1 × 10 ⁻³ mol, preferably 1 × 10 ⁻⁷ to 1 × 10 ⁻⁵ mol, more preferably 1 × 10 ⁻⁸ mol, per mol.
It is used in an amount of 10 ^{-7 to} 3 × 10 ^-6 mol. (a) When a catalyst selected from an alkali metal compound and an alkaline earth metal compound is used in such an amount, the polymerization activity can be maintained high, and the hue, heat resistance, water resistance, and weather resistance are excellent, and long-term A copolycarbonate having excellent melt stability can be obtained. In addition, in such an amount, an acidic compound (described below) is added in an amount that does not adversely affect the properties of the obtained copolycarbonate, and the basicity of these compounds is sufficiently neutralized or weakened. Can be.

In this production method, (a)
And (b) a nitrogen-containing basic compound and / or
(c) Boric acid compounds can be used.

As the nitrogen-containing basic compound (b), for example, a nitrogen-containing basic compound which is easily decomposable or volatile at a high temperature can be mentioned. Specifically, the following compounds can be mentioned. it: tetramethylammonium hydroxide (Me ₄ NOH, Me = methyl, hereinafter the same), tetraethylammonium hydroxide (Et ₄ NOH, Et = ethyl, hereinafter the same), tetrabutylammonium hydroxide (Bu ₄ NOH, Bu = butyl , The same applies hereinafter), trimethylbenzylammonium hydroxide (φ-CH ₂ (Me) ₃ NOH, φ =
Ammonium hydroxides having an alkyl, aryl, araryl group or the like such as phenyl); tertiary amines such as trimethylamine, triethylamine, dimethylbenzylamine, triphenylamine, trioctylamine, tridodecylamine or trioctadecylamine; R ₂ NH (where R is an alkyl group such as methyl and ethyl, and an aryl group such as phenyl and toluyl)
A primary amine represented by RNH ₂ (where R is as defined above); a pyridine such as 4-dimethylaminopyridine, 4-diethylaminopyridine, 4-pyrrolidinopyridine; Imidazoles such as -methylimidazole, 2-phenylimidazole and 2-dimethylaminoimidazole; ammonia; tetramethylammonium borohydride (Me ₄ NBH ₄ ), tetrabutylammonium borohydride (Bu ₄ NBH ₄ ), tetra Butyl ammonium tetraphenyl borate (Bu ₄ NBPh
_4), tetramethylammonium tetraphenylborate (Me ₄ NBPh ₄₎ basic salts, such as. Among them, tetraalkylammonium hydroxides, particularly tetraalkylammonium hydroxides for electronic use having few metal impurities are preferably used.

(B) The nitrogen-containing basic compound is preferably 1 × 10 ^{−6 with} respect to 1 mol of the total amount of the aromatic dihydroxy compound.
１1 × 10 ^-1 mol, more preferably 1 × 10 ^-5 to 1 × 10 ^-2 mol. When (b) is used in such an amount, the transesterification reaction and the polymerization reaction proceed at a sufficient rate, and a copolycarbonate excellent in hue, heat resistance, water resistance and the like can be obtained, which is preferable.

The catalyst obtained by combining (a) a catalyst selected from an alkali metal compound and an alkaline earth metal compound with (b) a nitrogen-containing basic compound has excellent heat resistance and water resistance and improved color tone. A high molecular weight copolycarbonate having excellent transparency can be produced with high polymerization activity.

Examples of the boric acid compound (c) include boric acid and boric acid esters. As the borate ester, a borate ester represented by the following general formula is used.

[0044]

Embedded image B (OR) _n (OH) _3-n (wherein R is an alkyl group such as methyl and ethyl, an aryl group such as phenyl, and n is 1, 2 or 3) Specific boric acid esters include, specifically, trimethyl borate, triethyl borate, tributyl borate,
Examples include trihexyl borate, triheptyl borate, triphenyl borate, tolyl borate, and trinaphthyl borate. (c) The boric acid compound is preferably from 1 × 10 ⁻⁸ to 1 based on 1 mol of the total amount of the aromatic dihydroxy compound.
× 10 ^-1 mol, more preferably 1 × 10 ^-7 to 1 × 10 ^-2 mol,
More preferably, it is used in an amount of 1 × 10 ^-6 to 1 × 10 ^-4 mol. (c) When boric acid or boric acid ester is used in such an amount, a molecular weight is hardly reduced at a high temperature, and a copolycarbonate excellent in hue, heat resistance and water resistance is obtained, which is preferable.

Particularly when (a) a catalyst selected from an alkali metal compound and an alkaline earth metal compound and (b) a large amount of a nitrogen-containing basic compound are used, (c) a three-part mixture further containing a boric acid compound The catalyst of the combination consisting of has good transparency, heat resistance, water resistance and color tone, and can produce a high molecular weight copolycarbonate with high polymerization activity.

The polycondensation reaction between an aromatic dihydroxy compound and a carbonic acid diester in the presence of a catalyst can be carried out under the same conditions as conventionally known polycondensation reaction between an aromatic dihydroxy compound and a carbonic acid diester. .

Specifically, the first-stage reaction is usually carried out at 80 to
The reaction is carried out at a temperature of 250 ° C., preferably 100 to 230 ° C., more preferably 120 to 190 ° C., usually at 0 to 5 hours, preferably 0 to 4 hours, more preferably 0 to 3 hours under normal pressure, and aromatic dihydroxy The compound is reacted with the carbonic acid diester. Then, the reaction temperature is increased while reducing the pressure of the reaction system to carry out the reaction between the aromatic dihydroxy compound and the carbonic acid diester, and finally, the aromatic dihydroxy compound is heated at a temperature of 240 to 320 ° C. under a reduced pressure of 5 mmHg or less, preferably 1 mmHg or less. A polycondensation reaction between the compound and a carbonic acid diester is performed.

The above-mentioned polycondensation reaction may be carried out continuously or batchwise. The reaction apparatus used for performing the above reaction may be a tank type, a tube type, or a tower type.

In this production method, as compared with the interfacial polycondensation method using phosgene, a uniform and stable branched polycarbonate can be obtained without gel formation during polymerization.

The above-described method for producing a copolycarbonate has the advantage that a copolycarbonate can be produced at a lower cost than the interface method, and that there is no need to use a substance that causes environmental pollution such as phosgene as a raw material. .

The (A) copolycar used in the present invention
It is preferable that the content of the alkali metal compound and / or alkaline earth metal compound is 1 ppm or less, the content of chlorine is 0.1 ppm or less, and the content of other metals is 0.1 ppm or less.

(A) Copolycarbonate used in the present invention
When the compound contains an alkali metal compound and / or an alkaline earth metal compound, the compound preferably further contains an acidic compound.

As long as the acidic compound can neutralize or weaken the alkali metal compound or alkaline earth metal compound remaining in the production of the copolycarbonate, even if it is a Lewis acid compound, it can be used as a Bronsted acid compound. It may be a compound or an ester of an acid containing a sulfur atom.

The acidic compound has a pK in an aqueous solution at 25 ° C.
a is preferably 3 or less. By using an acidic compound having such a pKa value, the alkali metal or alkaline earth metal used as a catalyst can be neutralized (or weakened), and the obtained copolycarbonate can be stabilized. There is an advantage.

As the Lewis acid compound, specifically, boron compounds such as zinc borate and boron phosphate; B (O
CH ₃ ) ₃ , B (OEt) ₃ , B (OPh) ₃ and other borate esters (Et represents ethyl and Ph represents phenyl); aluminum compounds such as aluminum stearate and aluminum silicate; zirconium carbonate Zirconium compounds such as alkoxide zirconium and zirconium hydroxycarboxylate; gallium compounds such as gallium phosphide and gallium antimonide; germanium compounds such as germanium oxide and organic germanium;
Tetra or hexaorganotin, PhOSn (Bu)
Tin compounds such as ₂ OSn (Bu) ₂ OPh (where,
Ph represents phenyl, Bu represents butyl); antimony compounds such as antimony oxide and alkylantimony; bismuth compounds such as bismuth oxide and alkylbismuth;
Zinc compounds such as (CH ₃ COO) ₂ Zn and zinc stearate; and titanium compounds such as alkoxytitanium and titanium oxide.

Specific examples of the Bronsted acid compound include phosphoric acid, phosphorous acid, hypophosphorous acid, pyrophosphoric acid, polyphosphoric acid, boric acid, hydrochloric acid, hydrobromic acid, sulfuric acid, sulfurous acid,
Adipic acid, azelaic acid, dodecanoic acid, L-ascorbic acid, aspartic acid, benzoic acid, formic acid, acetic acid, citric acid, glutamic acid, salicylic acid, nicotinic acid, fumaric acid, maleic acid, oxalic acid, benzenesulfinic acid, toluenesulfinic acid And sulfonic acid compounds such as benzenesulfonic acid, p-toluenesulfonic acid, trifluoromethanesulfonic acid, naphthalenesulfonic acid, sulfonated polystyrene, and methyl acrylate-sulfonated styrene copolymer.

Examples of the acid ester containing a sulfur atom include:
Specifically, pKa of an acid residue portion such as methyl, ethyl, butyl, octyl or phenyl ester of dimethyl sulfate, diethyl sulfate, p-toluenesulfonic acid, or methyl, ethyl, butyl, octyl or phenyl ester of benzenesulfonic acid is Up to three compounds are used.

Among such acidic compounds, acidic compounds containing a sulfur atom, a phosphorus atom and the like are preferred, and acidic compounds containing a sulfur atom are particularly preferred.

The acidic compound as described above may be present in the copolycarbonate in an amount capable of neutralizing (a) an alkaline compound such as an alkali metal compound or an alkaline earth metal compound or of weakening the influence thereof. What is necessary is just to contain. For this purpose, (a) 0.01 mol per mol of the total of the alkali metal compound and the alkaline earth metal compound is used.
To 500 mol, preferably 0.1 to 100 mol, more preferably 0.1 to 50 mol, particularly preferably 0.5 to 30 mol. In particular, when the acidic compound is a Lewis acid or a Bronsted acid having a pKa greater than 3, preferably 0.1 to 50 mol, more preferably 0.1 to 3 mol.
0 moles and the acidic compound has a pK of 3 or less.
When the ester is a Bronsted acid having a or an acid containing a sulfur atom, it is preferably used in an amount of 0.1 to 15 mol, more preferably 0.1 to 7 mol.

The (A) copolycarbonate used in the present invention may optionally contain an acidic compound together with a copolycarbonate.
It may contain from 5 to 1000 ppm of water relative to the bone. By adding water in such an amount, the neutralization efficiency of the acidic compound with respect to the catalyst is increased, and the heat stability at the time of melting, the retention stability such as hue stability, and the hue, transparency, water resistance, and weather resistance are improved. Further improve.

The optical copolycarbonate resin composition of the present invention contains (B) an ester of an aliphatic carboxylic acid and a polyhydric alcohol together with the above-mentioned component (A). Esters can be partial esters and / or full esters.

The aliphatic carboxylic acid is not particularly limited, and both saturated and unsaturated aliphatic carboxylic acids can be used. For example, a hydrogenated animal oil can be used. As the aliphatic carboxylic acid,
Saturated monovalent fatty acids are preferred, and those having 12 to 24 carbon atoms are particularly preferred. When the carbon number is less than the above range, the thermal stability of the produced resin composition tends to be inferior to those in the above range, and gas is generated. On the other hand, when the carbon number is larger than the above range, the releasability of the resin composition tends to be inferior to those in the above range. Specific examples of the aliphatic carboxylic acid include dodecylic acid, myristic acid, pentadecylic acid, palmitic acid, heptadecylic acid, stearic acid, nonadecanoic acid, arachinic acid, behenic acid, and lignoceric acid.

The polyhydric alcohol is not particularly limited, and any of divalent, trivalent, tetravalent, pentavalent, hexavalent and the like can be used. Examples thereof include ethylene glycol, glycerin, trimethylolpropane and pentaerythritol. And glycerin is particularly preferred.

The ester of the aliphatic carboxylic acid and the polyhydric alcohol used in the present invention can be obtained by a conventional esterification reaction.

(B) The ester of the aliphatic carboxylic acid and the polyhydric alcohol is used in an amount of 0.01 part by weight or more, preferably 0.04 part by weight or more, and Parts by weight or less, preferably 0.08
It is blended in an amount of not more than part by weight. If the amount is larger than the above upper limit, the thermal stability of the resin composition is deteriorated. If the amount is smaller than the above lower limit, it is difficult to obtain sufficient releasability and accurate transfer of pits.

The optical copolycarbonate resin composition of the present invention can be used for a wide variety of applications. Such compositions include:
A heat stabilizer, an antistatic agent, a slip agent, an antiblocking agent, a lubricant, an antifogging agent, a natural oil, a synthetic oil, a wax and the like may be contained within a range not to impair the object of the present invention.

Specific examples of such heat stabilizers include phenol stabilizers, organic thioether stabilizers,
An organic phosphorus stabilizer, a hindered amine stabilizer, an epoxy stabilizer and the like can be mentioned.

Examples of the phenolic stabilizer include n-octadecyl-3- (4-hydroxy-3 ′, 5′-di-t-butylphenyl) propionate and tetrakis [methylene-3- (3 ′,
5'-di-t-butyl-4-hydroxyphenyl) propionate] methane, 1,1,3-tris (2-methyl-4-hydroxy
-5-t-butylphenyl) butane, distearyl (4-hydroxy-3-methyl-5-t-butyl) benzylmalonate,
4-hydroxymethyl-2,6-di-t-butylphenol and the like.

Examples of the thioether-based stabilizer include dilauryl thiodipropionate, distearyl thiodipropionate, dimyristyl-3,3'-thiodipropionate, ditridecyl-3,3'-thiodipropionate, Pentaerythritol-tetrakis- (β-lauryl-thiopropionate);

As the phosphorus-based stabilizer, for example, bis (2,4-
Arylalkyl phosphites such as di-t-butylphenyl) pentaerythrityl diphosphite, diphenyldecyl phosphite, diphenylisooctyl phosphite, phenylisooctyl phosphite, 2-ethylhexyl diphenyl phosphite; trimethyl phosphite, triethyl phosphite Phytite, tributyl phosphite, trioctyl phosphite, trinonyl phosphite, tridecyl phosphite, trioctadecyl phosphite, distearyl pentaerythrityl diphosphite, tris (2-chloroethyl) phosphite, tris (2,3- Trialkyl phosphites such as dichloropropyl) phosphite; tricycloalkyl phosphites such as tricyclohexyl phosphite; triphenyl phosphite, tricresyl Triaryl phosphites such as phosphite, tris (ethylphenyl) phosphite, tris (2,4-di-t-butylphenyl) phosphite, tris (nonylphenyl) phosphite and tris (hydroxyphenyl) phosphite; trimethyl phosphate , Triethyl phosphate, tributyl phosphate, trioctyl phosphate, tridecyl phosphate, trioctadecyl phosphate, distearyl pentaerythrityl diphosphate, tris (2-chloroethyl) phosphate, tris (2,3-dichloropropyl)
Trialkyl phosphates such as phosphate; tricycloalkyl phosphates such as tricyclohexyl phosphate; and triaryl phosphates such as triphenyl phosphate, tricresyl phosphate, tris (nonylphenyl) phosphate, and 2-ethylphenyl diphenyl phosphate.

The hindered amine stabilizers include
For example, bis (2,2,6,6-tetramethyl-4-piperidyl) sebacate, bis (1,2,2,6,6-pentamethyl-4-piperidyl) sebacate, 1- [2- {3- (3 , 5-Di-t-butyl-4-hydroxyphenyl) propionyloxydiethyl] -4-
{3- (3,5-di-t-butyl-4-hydroxyphenyl) propionyloxy} -2,2,6,6-tetramethylpiperidine,
8-benzyl-7,7,9,9-tetramethyl-3-octyl-1,2,3-
Triazaspiro [4,5] undecane-2,4-dione, 4-benzoyloxy-2,2,6,6-tetramethylpiperidine, 2-
Bis (1,2,2,6,6-pentamethyl-4-piperidyl) (3,5-di-t-butyl-4-hydroxybenzyl) -2-n-butylmalonate, Tetrakis (2,2,6 , 6-tetramethyl-4-piperidyl) 1,2,3,4-butanetetracarboxylate.

These are used alone or in combination. These heat stabilizers may be added in a solid state or in a liquid state.

The heat stabilizer is used in an amount of usually 0.001 to 5 parts by weight, preferably 0.01 to 0.3 parts by weight, based on 100 parts by weight of the copolycarbonate (A).

In the present invention, the other additives as described above, especially the heat stabilizer, are used in the same manner as in the method of adding an acidic compound to the copolycarbonate, while the copolycarbonate is cooled from the final polymerization vessel and melted while being pelletized. It is preferable to add it while it is in a state, so that a copolycarbonate composition having a small number of heat histories during production can be obtained. In addition, when heat treatment is performed again such as extrusion molding and pelletizing, the copolycarbonate composition contains a heat stabilizer, so that thermal decomposition can be suppressed.

The method for producing the resin composition of the present invention is not particularly limited, and ordinary methods can be used satisfactorily. However, the melt mixing method is generally preferred. The use of small amounts of solvents is possible but generally not necessary. Examples of the apparatus include an extruder, a Banbury mixer, a roller, a kneader, etc., which are operated batchwise or continuously. The order of mixing the components is not particularly limited.

[0076]

EXAMPLES Next, the present invention will be described specifically with reference to examples, but the present invention is not limited to these examples.

The composition and physical properties of the copolycarbonate obtained in the following examples were measured as follows. 1) Analysis of Structural Units of Copolycarbonate By measuring ¹³ C-NMR, the structural units derived from the aromatic dihydroxy compound in the resin and the ratio thereof were examined. The measurement conditions of ¹³ C-NMR were as follows: Measurement device: ¹³ C-NMR GX-270 (manufactured by JEOL Ltd.) Measurement solvent: CDCl ₃ Standard substance: CDCl ₃ (77.00 ppm) Sample preparation Method: 0.4 g of the polymer was dissolved in ₃ ml of CDCl ₃ .

Measurement conditions: 110 MHz, integrated 30,000 times 2) Viscosity average molecular weight From intrinsic viscosity [η] measured with methylene chloride (0.5 g / dl) at 20 ° C. using an Ubbelohde viscometer, the following formula was obtained.

[0079]

[Η] = 1.23 × 10 ⁻⁴ × M ^0.83 (M = viscosity average molecular weight) 3) Melt flow rate (MFR) According to the method of JIS K-7210, at a temperature of 250 ° C,
It was measured at a load of 1.2 kg. 4) Compact disk formability The formability (stringing phenomenon) of each compact disk molding machine under each molding condition was confirmed. 100 shot continuous molding was performed. 5) Optical distortion of compact disk The birefringence of the disk (12 cm diameter) obtained by molding was measured using a birefringence measuring device. 6) Transferability of compact disk The surface of the disk (12 cm diameter) obtained by molding is
The pit shape was confirmed by observation with an optical microscope (magnification: 800). The unclear number of the 10 sheets was examined.

Production Example 1 Monocarboxylated bisphenol A [that is, 2- (4-hydroxy) was purified by carboxylation using a potassium salt of bisphenol A with carbon dioxide gas, followed by purification by recrystallization using a toluene solvent. Phenyl) -2-
(3'-carboxy-4'-hydroxyphenyl) propane]
I got This monocarboxylated bisphenol A was esterified with a large excess of diphenyl carbonate, and then purified by column purification to a purity of 99% or more (HPLC
Analysis) of 2- (4-hydroxyphenyl) -2- (3'-
Phenoxycarbonyl-4′-hydroxyphenyl) propane was obtained.

0.44 mmol of bisphenol A (manufactured by Nippon GE Plastics Co., Ltd.)
0.433 mol of (4-hydroxyphenyl) -2- (3'-phenoxycarbonyl-4'-hydroxyphenyl) propane and 0.46 of diphenyl carbonate (manufactured by Any)
A kilomol was charged into a 250-liter stirred tank, and after purging with nitrogen, it was dissolved at 140 ° C.

Then, the temperature was raised to a temperature of 180 ° C., and tetramethylammonium hydroxide was added as a catalyst to a temperature of 0.1 ° C.
11 moles and 0.00044 moles of sodium hydroxide (1 × 10 ^-6 moles / mole-bisphenol A) were added.
Stirred for minutes.

Next, the temperature was raised to 210 ° C. and gradually lowered to 200 mmHg.
At the same time as the temperature was raised to 40 ° C., the temperature and pressure were kept constant by gradually lowering the pressure to 15 mmHg, and the amount of phenol distilled out was measured. When there was no more phenol distilled out, the pressure was returned to atmospheric pressure with nitrogen. The time required for the reaction was 1 hour.
The intrinsic viscosity number [η] of the obtained reaction product is 0.15 dl /
g.

Next, the pressure of the reaction product was increased by a gear pump, and the reaction product was sent to a centrifugal thin film evaporator to proceed the reaction. The temperature and pressure of the thin film evaporator were controlled at 270 ° C. and 2 mmHg, respectively. From the bottom of the evaporator, use a gear pump at 290 ° C.
Biaxial horizontal stirring polymerization tank controlled at 2 mmHg (L
/ D = 3, stirring blade rotation diameter 220 mm, internal volume 80 liter) at a rate of 40 kg / hour and polymerization for a residence time of 30 minutes.

¹³ C-NMR of the polymer thus obtained
From the measurement results, this polymer is a copolycarbonate having, as a component derived from an aromatic dihydroxy compound, structural units represented by the following formulas [V] and [VI] in a molar ratio of 99.9 to 0.1. It was confirmed.

[0086]

Embedded image

[0087]

Embedded image The charts of ¹³ C-NMR are shown in FIGS. 1 and 2, and the assignment of each peak is shown in FIG. The peaks derived from the carbon atoms at positions and were observed at 123.07 ppm and 162.91 ppm, respectively.

The viscosity average molecular weight of this copolycarbonate determined from the limiting viscosity number [η] was 15,500.

Next, in the molten state, the copolycarbonate was twin-screw extruded with a gear pump (L / D = 17.
5, barrel temperature 285 ° C.), and based on the copolycarbonate, 1.8 ppm of butyl p-toluenesulfonate;
50 ppm of distilled water was kneaded, made into a strand through a die, and cut into a pellet by a cutter. The MFR was measured and found to be 9.5 g / 10 minutes.

The above additive-containing copolycarbonate is
-Called PC1.

Preparation Example 2 In Preparation Example 1, bisphenol A and 2- (4-hydroxyphenyl) -2- (3'-phenoxycarbonyl-4'-
The molar ratio of hydroxyphenyl) propane was 9
A copolycarbonate was produced in the same manner as in Production Example 1 except that the ratio was changed to 9.95 to 0.05.

¹³ C-NMR of the polymer thus obtained
From the measurement results, this polymer is a copolycarbonate having, as a component derived from an aromatic dihydroxy compound, the structural units represented by the above formulas [V] and [VI] in a molar ratio of 99.95 to 0.05. I understand. That is, according to the results of the ¹³ C-NMR analysis, the peaks (123.07 ppm and 162.91 ppm) in the ¹³ C-NMR chart of the polymer produced in Production Example 1
) Was の of the peak intensity of Production Example 1. Table 1 shows the viscosity average molecular weight of the copolycarbonate obtained from the intrinsic viscosity number [η].

The copolycarbonate obtained above is
Additives were added in the same manner as in Production Example 1 to produce pellets. The MFR value was measured for this. Table 1 shows the results
Shown in

The above-mentioned additive-containing copolycarbonate is
-Called PC2.

Preparation Example 3 In Preparation Example 1, bisphenol A and 2- (4-hydroxyphenyl) -2- (3′-phenoxycarbonyl-4′-
(Hydroxyphenyl) propane:
A copolycarbonate was produced in the same manner as in Production Example 1 except that the ratio was changed to 99: 0.01.

¹³ C-NMR of the polymer thus obtained
From the measurement results, this polymer is a copolycarbonate having, as a component derived from an aromatic dihydroxy compound, the structural units represented by the above formulas [V] and [VI] in a molar ratio of 99.99 to 0.01. I understand. That is, according to the results of the ¹³ C-NMR analysis, the peaks (123.07 ppm and 162.91 ppm) in the ¹³ C-NMR chart of the polymer produced in Production Example 1
) Was 1/10 of the peak intensity of Production Example 1. Table 1 shows the viscosity average molecular weight of the copolycarbonate obtained from the intrinsic viscosity number [η].

Further, the copolycarbonate obtained above is
Additives were added in the same manner as in Production Example 1 to produce pellets. The MFR value was measured for this. Table 1 shows the results
Shown in

The above additive-containing copolycarbonate is
-Called PC3.

Production Example 4 In Production Example 1, bisphenol A and 2- (4-hydroxyphenyl) -2- (3'-phenoxycarbonyl-4'-
(Hydroxyphenyl) propane:
A copolycarbonate was produced in the same manner as in Production Example 1 except that 7: 0.3 was used.

¹³ C-NMR of the polymer thus obtained
From the measurement results, this polymer is a copolycarbonate having, as a component derived from an aromatic dihydroxy compound, the structural units represented by the above formulas [V] and [VI] in a molar ratio of 99.7 to 0.3. I understand. That is, ¹³
As a result of the C-NMR analysis, the intensity of the peaks (123.07 ppm and 162.91 ppm) in the ¹³ C-NMR chart of the polymer produced in Production Example 1 was three times the peak intensity of Production Example 1. there were. Table 1 shows the viscosity average molecular weight of the copolycarbonate obtained from the intrinsic viscosity number [η].

Further, to the copolycarbonate obtained above,
Additives were added in the same manner as in Production Example 1 to produce pellets. The MFR value was measured for this. Table 1 shows the results
Shown in

The above additive-containing copolycarbonate is
-Called PC4.

Preparation Example 5 In Preparation Example 1, bisphenol A and 2- (4-hydroxyphenyl) -2- (3′-phenoxycarbonyl-4′-
(Hydroxyphenyl) propane:
A copolycarbonate was produced in the same manner as in Production Example 1 except that the ratio was changed to 995 to 0.005.

¹³ C-NMR of the polymer thus obtained
From the measurement results, this polymer is a copolycarbonate having, as a component derived from an aromatic dihydroxy compound, the structural units represented by the above formulas [V] and [VI] in a molar ratio of 99.995 to 0.005. I understand. That is, according to the results of the ¹³ C-NMR analysis, the peaks of and (123.07 ppm and 162.91 pp) in the ¹³ C-NMR chart of the polymer produced in Production Example 1 were obtained.
m) was 1/20 of the peak intensity of Production Example 1. Table 1 shows the viscosity average molecular weight of the polycarbonate obtained from the intrinsic viscosity number [η].

Further, to the copolycarbonate obtained above,
Additives were added in the same manner as in Production Example 1 to produce pellets. The MFR value was measured for this. Table 1 shows the results
Shown in

The above additive-containing copolycarbonate is
-Called PC5.

Production Example 6 A polycarbonate was produced in the same manner as in Production Example 1 except that 2- (4-hydroxyphenyl) -2- (3′-phenoxycarbonyl-4′-hydroxyphenyl) propane was not used. .

¹³ C-NMR of the polymer thus obtained
From the measurement results, it was found that this polymer was a polycarbonate having only a unit derived from bisphenol A as a component derived from an aromatic dihydroxy compound. That, ¹³ C-NMR results of the analysis of, ¹³ C-NMR and the chart of the peaks of the polymer prepared in Preparation Example 1 (123.07ppm and 16
2.91 ppm) was not observed. Table 1 shows the viscosity average molecular weight of the polycarbonate obtained from the intrinsic viscosity number [η].

Further, an additive was added to the polycarbonate obtained above in the same manner as in Production Example 1 to prepare pellets. The MFR value was measured for this. Table 1 shows the results.

The above additive-containing polycarbonate was prepared using PC-1
Called.

Examples 1 to 3 and Comparative Examples 1 to 3 (1) Production of resin composition (co) polycarbonate containing additives (co-PC1 to co-PC5, PC-1) produced in Production Examples 1 to 6 To 100 parts by weight of each, 0.05 parts by weight of stearic acid monoglyceride (SMG) was blended and melt-kneaded at 260 ° C. using a single screw extruder (L / D = 17.5) to prepare pellets. Table 2 shows the composition of each composition. (2) Compact disk molding The pellets obtained in (1) were injection molded under the conditions shown in Table 3 to form a compact disk. The moldability (the presence or absence of stringing) at that time was determined, and the results are shown in Table 4. (3) Confirmation of optical distortion The pellet obtained in (1) was injection-molded under the condition 2 shown in Table 3 to form a compact disc (12 cm diameter).
This was measured for birefringence, and the results are shown in Table 5. (4) Confirmation of Transferability The pellet obtained in (1) was injection-molded under the condition 2 shown in Table 3 to form a compact disc (12 cm diameter).
Regarding this, the transferability of the pit was confirmed. Table 6 shows the results.

Comparative Example 4 (1) Pellets of a resin composition were prepared in the same manner as in (1) of Example 1, except that only co-PC1 was used without mixing stearic acid monoglyceride. (2) Compact disk molding The pellets obtained in (1) were injection molded under the conditions shown in Table 3 to form a compact disk. The moldability (the presence or absence of stringing) at that time was determined, and the results are shown in Table 4. (3) Confirmation of optical distortion The pellet obtained in (1) was injection-molded under the condition 2 shown in Table 3 to form a compact disc (12 cm diameter).
This was measured for birefringence, and the results are shown in Table 5. (4) Confirmation of Transferability The pellet obtained in (1) was injection-molded under the condition 2 shown in Table 3 to form a compact disc (12 cm diameter).
Regarding this, the transferability of the pit was confirmed. Table 6 shows the results.

[0113]

[Table 1]

[0114]

[Table 2]

[0115]

[Table 3]

[0116]

[Table 4]

[0117]

[Table 5] * R indicates the radial distance from the center of the disk.

[0118]

[Table 6] Table 6 ─────────────────────────────────── Example Comparative Example 1 2 3 1 2 3 4 転 写 Transferability Number of unclear pit shapes 0/10 0/10 0/10 8/10 0/10 0/10 6/10 ──────────────────────────────── ───

[0119]

By using the optical copolycarbonate resin composition of the present invention, an optical molded product having excellent characteristics such as optical distortion and pit transferability can be stably obtained under a wide range of molding conditions. Therefore, the optical copolycarbonate resin composition of the present invention is industrially very useful.

[Brief description of the drawings]

FIG. 1 ¹³ C of copolycarbonate produced in Production Example 1
It is a chart which shows the result of -NMR analysis.
Shows the range of 40 ppm.

FIG. 2 shows ¹³ C of copolycarbonate produced in Production Example 1.
-It is a chart which shows the result of NMR analysis, 140-1.
Shows the range of 70 ppm.

FIG. 3 shows ¹³ C of copolycarbonate produced in Production Example 1.
-Indicates the assignment of each peak in a chart showing the results of NMR analysis.

────────────────────────────────────────────────── (5) References JP-A-4-175368 (JP, A) US Patent 4,701,516 (US, A) (58) Fields investigated (Int. Cl. ⁷ , DB name) C08G 64 / 00-64/42

Claims (6)

(57) [Claims] 1. A copolycarbonate obtained by copolymerizing (A) two or more aromatic dihydroxy compounds and a compound capable of introducing a carbonic acid bond, wherein (1) an aromatic dihydroxy compound As the derived component unit, the following formula [I]: (In the formula, X is ^{- (R 3 -) C (} -R 4) -, - C
^{(= R 5) -, -} O -, - S -, - SO- or -SO
₂ --wherein R ³ and R ⁴ are a linear, branched or cyclic monovalent hydrocarbon group having 1 to 15 carbon atoms which may be substituted with a hydrogen atom or halogen, and R ⁵ is Is a linear, branched or cyclic divalent hydrocarbon group having 1 to 15 carbon atoms which may be substituted with halogen, and R ¹ and R ² may be the same or different A straight-chain, branched or cyclic hydrocarbon group having 1 to 10 carbon atoms which may be substituted with a halogen, or a halogen atom, m and n each represent the number of substituents, and each independently represents 0 And a structural unit represented by the following formula [II]: (In the above formula, Y is-(R3 ^' -) C (-R4 ^' )-, -C
(= R5 ^' )-, -O-, -S-, -SO- or -SO
₂ --wherein R ^{3 ′} and R ^{4 ′} are a hydrogen atom or a linear, branched or cyclic monovalent hydrocarbon group having 1 to 15 carbon atoms which may be substituted by a halogen atom; ^{5 ′} is a linear, branched or cyclic divalent hydrocarbon group having 1 to 15 carbon atoms which may be substituted with halogen, and R ⁷ and R ⁸ may be the same or different. Each may be a linear, branched or cyclic hydrocarbon group having 1 to 10 carbon atoms which may be substituted with a halogen, or a halogen atom, p and q represent the number of substituents, and p is Is an integer of 0 to 4, and q is an integer of 0 to 3)
And in shown a structural unit, wherein with respect to the structural units to 1 mol represented by [I], the structural unit 8 × 10 ^-5 of the formula [II]
(2) 100 parts by weight of a copolycarbonate having a viscosity average molecular weight of 12,000 to 18,000, and (B) an ester of an aliphatic carboxylic acid and a polyhydric alcohol in an amount of from 0.01 to 1.5 × 10 ^-3 mol. An optical copolycarbonate resin composition containing 0.1 to 0.1 parts by weight. 2. In the above formula [I] of the component (A), X is a linear or branched alkylene, and the above formula [I]
The resin composition according to claim 1, wherein in I], Y is a linear or branched alkylene. 3. The component (A), wherein the aromatic dihydroxy compound for introducing the structural unit represented by the formula [I] is 2,2-bis (4-hydroxyphenyl) propane. 3. The resin composition according to 2. 4. In the component (A), the aromatic dihydroxy compound for introducing the structural unit represented by the formula [II] is 2- (4-hydroxyphenyl) -2- (3′-carboxy-4). A compound selected from '-hydroxyphenyl) propane and 2- (4-hydroxyphenyl) -2- (3'-phenoxycarbonyl-4'-hydroxyphenyl) propane.
4. The resin composition according to any one of 3. 5. The component (B) wherein the aliphatic carboxylic acid is a saturated monovalent fatty acid having 12 to 24 carbon atoms.
5. The resin composition according to any one of items 4 to 4. 6. In component (B), the polyhydric alcohol is selected from ethylene glycol, glycerin, trimethylolpropane and erythritol.
The resin composition according to any one of claims 1 to 5.