JP2002053653A - Method for producing aromatic polycarbonate - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide an industrially favorable method for producing a high- quality aromatic polycarbonate good in color and slightly causing discoloration even at high temperatures of >=380 deg.C with a small reduction in molecular weight when the aromatic polycarbonate is produced by a melt polycondensation method. SOLUTION: This method for producing the aromatic polycarbonate comprises using a diaryl carbonate having (a) <=200 wt.ppm moisture content, (b) <=1 wt.ppm copper content and (c) <=1 wt.ppm (p-phenoxyphenyl) (phenyl) carbonate content is used a.s the diaryl carbonate in the method for producing the aromatic polycarbonate by polymerizing an aromatic dihydroxy compound with the diaryl carbonate in a molten state.

Description

DETAILED DESCRIPTION OF THE INVENTION

[0001]

[0001] The present invention relates to a method for producing an aromatic polycarbonate.

[0002]

2. Description of the Related Art In recent years, aromatic polycarbonates have been widely used in many fields as engineering plastics having excellent heat resistance, impact resistance and transparency. However, polycarbonates produced by the conventionally used phosgene method use toxic phosgene at the time of production and contain residual methylene chloride which affects the heat stability of the polycarbonate and mold corrosion during molding. In recent years, polycarbonates obtained by the transesterification method have been reviewed.

[0003] Transesterification polycarbonates generally have poor color, and there has been a long demand for improved coloring. However, if the color at the time of polycarbonate production is only good, it cannot be said that the quality as a molding material is satisfied, and among polycarbonates, aromatic polycarbonate is inferior in molding fluidity, so a good molded appearance is required. In applications as a molding material for injection molding and as a molding material for molded articles requiring high transparency, molding is generally carried out at a higher temperature than ordinary resins. The applications as required molding materials for precision molded products are expanding, and aromatic polycarbonates with little coloring even when molded at high temperatures are strongly desired. In optical disc applications that require high cycleability of molding, molding is performed particularly at high temperatures, so there were problems such as resin coloring and molecular weight reduction during molding interruption such as mold cleaning. .

[0004] That is, there has been a strong demand for an aromatic polycarbonate which has little coloring and a small molecular weight reduction even at a high temperature of 380 ° C or higher. When producing an aromatic polycarbonate by polymerizing in a molten state from an aromatic dihydroxy compound and a diaryl carbonate by a transesterification method, from the viewpoint of improving the coloration of the product, an application specifying the amount of a specific compound in the raw material has been filed. Many have been done.

For example, in Japanese Patent Application Laid-Open No. Hei 5-262873, the chlorine content based on chloroformate as an impurity contained in the carbonic diester is 30 ppm or less. In Japanese Patent Application Laid-Open No. Hei 6-179744, phenyl salicylate is used as the carbonic acid diester. , O-phenoxybenzoic acid and phenyl o-phenoxybenzoate are not substantially contained. JP-A-7-33866 discloses that a diaryl carbonate having a benzophenone derivative of 100 ppm or less is used, JP-A-7-62074. In the gazette, diaryl carbonate having an ester derivative of 100 ppm or less is used. In JP-A-8-59815, diphenyl carbonate containing substantially no phenyl o-methoxybenzoate and xanthone is used. Under (EP) -0677545A1 JP, salicylic acid derivatives, stannous ion, or the like using a carbonic acid diester without the one of methyl phenyl carbonate, defines the abundance of a particular compound in the diaryl carbonate.

In Japanese Patent Application Laid-Open No. 8-104747, the amount of an aromatic dihydroxy compound having a specific structure is 1
0 ppm by weight or more and 3% by weight or less;
No. 104748 discloses a specific bisphenol A derivative, a bisphenol A isomer, a chroman organic compound,
Total content of trisphenol I is 100 ppm or more and 10
Using bisphenol A that is not more than 00 ppm,
JP-A-11-310630 discloses the presence of a specific compound in an aromatic dihydroxy compound, such as using bisphenol A having a chroman organic compound content of 200 ppm or less and an iron content of 0.1 ppm or less. Specifies the amount. However, these inventions
Not always enough to improve color, and 38
Even at a high temperature of 0 ° C. or higher, it has not been possible to provide an aromatic polycarbonate with little coloring and little molecular weight reduction.

[0007]

SUMMARY OF THE INVENTION An object of the present invention is to provide an aromatic polycarbonate produced by a melt polycondensation method, which has a good color, has little coloring even at a high temperature of 380 ° C. or higher, and has a small molecular weight. It is an object of the present invention to provide an industrially preferable method for producing a novel aromatic polycarbonate.

[0008]

Means for Solving the Problems The present inventors have made intensive studies to solve the above-mentioned problems, and as a result, when producing an aromatic polycarbonate, the content of a specific component in diaryl carbonate was adjusted to a specific range. It has been found that the above object can be achieved by controlling the above-mentioned conditions, and the present invention has been completed.

That is, the present invention provides (1) a process for producing an aromatic polycarbonate which is polymerized in a molten state from an aromatic dihydroxy compound and a diaryl carbonate, wherein the diaryl carbonate is (a) having a water content of 2
(B) copper content is 1 weight pp
m or less, and (c) a content of (p-phenoxyphenyl) (phenyl) carbonate of 1 ppm by weight or less, a method for producing an aromatic polycarbonate,
(2) a diaryl carbonate having (a) a water content of 2
(B) copper content is 1 weight pp
m. or less, wherein the diaryl carbonate is a diaryl carbonate stored in a molten state at a temperature of 80 to 190 ° C. in a stainless steel container under a nitrogen atmosphere in a stainless steel container. (3) The method for producing an aromatic polycarbonate according to (2), wherein the stainless steel container is a container in which the liquid contact portion on the inner wall surface has been subjected to a washing treatment with phenol.

In the production of an aromatic polycarbonate by a melt polymerization method, usually, the raw material diaryl carbonate is not completely 100% pure but is derived from a method for producing a diaryl carbonate or a method for storing the produced diaryl carbonate. Contains various compounds. Diaryl carbonate is rarely used immediately after production, and is used after transportation and storage, so clarifying the effects of compounds that are mixed or generated during storage is an industrial process for producing aromatic polycarbonates. Is particularly important in doing so.

As a result of diligent studies by the present inventors, water mixed by moisture absorption, copper which is a catalyst component used in the production of diaryl carbonate, and diaryl carbonate formed during storage in a molten state (p-phenoxy) By making the content of (phenyl) (phenyl) carbonate all the specific value or less, the color of the aromatic polycarbonate product is surprisingly improved,
It has been revealed that the stability against coloring and molecular weight reduction at a high temperature of 380 ° C. or more is remarkably improved.

Hereinafter, the present invention will be described in detail. In the present invention, the aromatic dihydroxy compound is HO-
It is a compound represented by Ar-OH (wherein, Ar represents a divalent aromatic group). The aromatic group Ar is preferably, for example, -Ar ¹ -Y-Ar ^2- (wherein Ar ¹ and Ar
² independently represents a divalent carbocyclic or heterocyclic aromatic group having 5 to 70 carbon atoms, and Y represents 1 to 30 carbon atoms.
Represents a divalent substituted or unsubstituted alkane group. ) Is a divalent aromatic group.

In the divalent aromatic groups Ar ¹ and Ar ² ,
One or more hydrogen atoms having no adverse effect on the reaction, for example, a halogen atom, an alkyl group having 1 to 10 carbon atoms, an alkoxy group having 1 to 10 carbon atoms, a phenyl group,
It may be substituted by a phenoxy group, vinyl group, cyano group, ester group, amide group, nitro group, or the like. Preferred specific examples of the heterocyclic aromatic group include 1
And an aromatic group having a plurality of ring-forming nitrogen atoms, oxygen atoms or sulfur atoms.

Further, the divalent aromatic groups Ar ¹ and Ar ² are
For example, it represents a group such as substituted or unsubstituted phenylene, substituted or unsubstituted biphenylene, and substituted or unsubstituted pyridylene. The substituent here is as described above. The divalent alkane group Y is, for example, an organic group represented by the following chemical formula 1.

[0015]

Embedded image

(Wherein R ¹ , R ² , R ³ , and R ⁴ each independently represent hydrogen, an alkyl group having 1 to 10 carbon atoms,
10 alkoxy groups, a cycloalkyl group having 5 to 10 ring carbon atoms, a carbocyclic aromatic group having 5 to 10 ring carbon atoms,
Represents a carbocyclic aralkyl group having 6 to 10 carbon atoms. k is 3
And R ⁵ and R ⁶ are individually selected for each X and independently of one another, hydrogen or C 1 -C
And X represents carbon. R ¹ ,
In R ² , R ³ , R ⁴ , R ⁵ and R ⁶ , other substituents as long as one or more hydrogen atoms do not adversely affect the reaction,
For example, a halogen atom, an alkyl group having 1 to 10 carbon atoms,
It may be substituted by an alkoxy group having 1 to 10 carbon atoms, phenyl group, phenoxy group, vinyl group, cyano group, ester group, amide group, nitro group and the like. Examples of such a divalent aromatic group Ar include those represented by the following chemical formula 2.

[0017]

Embedded image

(Wherein R ⁷ and R ⁸ each independently represent a hydrogen atom, a halogen atom, an alkyl group having 1 to 10 carbon atoms, an alkoxy group having 1 to 10 carbon atoms, and a cycloalkyl having 5 to 10 ring carbon atoms) An alkyl group or a phenyl group, m and n
Is an integer of 1 to 4, and when m is 2 to 4, each R ⁷ may be the same or different, and n is 2 to 4
In this case, each R ⁸ may be the same or different. ) Further, the divalent aromatic group Ar is -Ar ¹
—Z—Ar ² — (wherein, Ar ¹ and Ar ² are as described above, and Z is a single bond or —O—, —CO—, —S—, and —S
Represents a divalent group such as O ₂ —, —SO—, —COO—, and —CON (R ¹ ) —. Here, R ¹ is as described above. ) May be used. Such 2
Examples of the valent aromatic group Ar include those represented by the following chemical formula 3.

[0019]

Embedded image (In the formula, R ⁷ , R ⁸ , m and n are as described above.)

Further, specific examples of the divalent aromatic group Ar include substituted or unsubstituted phenylene, substituted or unsubstituted naphthylene, and substituted or unsubstituted pyridylene. The aromatic dihydroxy compound used in the present invention may be a single kind or two or more kinds. A typical example of the aromatic dihydroxy compound is bisphenol A.

The diaryl carbonate used in the present invention is represented by the following chemical formula 4.

Embedded image (In the formula, Ar ³ and Ar ⁴ each represent a monovalent aromatic group.)

Ar ³ and Ar ^{4 each} represent a monovalent carbocyclic or heterocyclic aromatic group. In Ar ³ and Ar ⁴ , one or more hydrogen atoms have no adverse effect on the reaction. Substituents, for example, a halogen atom, an alkyl group having 1 to 10 carbon atoms, an alkoxy group having 1 to 10 carbon atoms, a phenyl group, a phenoxy group, a vinyl group, a cyano group, an ester group,
It may be substituted by an amide group, a nitro group or the like. Ar ³ and Ar ⁴ may be the same or different.

Representative examples of the monovalent aromatic groups Ar ³ and Ar ⁴ include a phenyl group, a naphthyl group, a biphenyl group and a pyridyl group. These may be substituted with one or more substituents described above. Preferred Ar
Examples of ³ and Ar ⁴ include, for example, those shown in Chemical Formula 5 below.

[0024]

Embedded image

Representative examples of diaryl carbonates include substituted or unsubstituted diphenyl carbonates represented by the following formula (6).

Embedded image (Wherein R ⁹ and R ¹⁰ are each independently a hydrogen atom, an alkyl group having 1 to 10 carbon atoms, an alkoxy group having 1 to 10 carbon atoms, a cycloalkyl group having 5 to 10 ring carbon atoms, or a phenyl group) In the formula, p and q are integers of 1 to 5, and when p is 2 or more, each R ⁹ may be different, and when q is 2 or more, each R ¹⁰ is Each may be different.)

Among the diphenyl carbonates,
Unsubstituted diphenyl carbonate, symmetric diaryl carbonates such as lower alkyl-substituted diphenyl carbonates such as ditolyl carbonate and di-t-butylphenyl carbonate are preferred, but unsubstituted diphenyl which is a diaryl carbonate having the simplest structure is particularly preferred. Carbonates are preferred. These diaryl carbonates may be used alone or in combination of two or more.

In the present invention, the water content of the diaryl carbonate is 200 ppm by weight or less. If the water content is more than 200 ppm by weight, the color of the resulting aromatic polycarbonate is deteriorated, and the product is easily colored at a high temperature of 380 ° C. or higher, and the molecular weight is greatly reduced. Although the reason is not clear, it is presumed that a combination of decomposition of the diaryl carbonate due to the presence of water and an isomerization reaction of the diaryl carbonate adversely affects the stability of the aromatic polycarbonate at high temperatures. The water content of the diaryl carbonate is preferably 100 ppm by weight or less, more preferably 50 ppm by weight or less. The lower limit of the water content is not particularly limited, and the water content may be lower than 0.01 ppm by weight. The effect of improving is small.

As a method of controlling the water content in the diaryl carbonate to the above-mentioned range, there are a method of avoiding moisture absorption during transportation and storage, and a method of absorbing moisture, which is the upper limit of 200 wt.
When the water content becomes higher than pm, a method of performing a dehydration operation by distillation or the like and then using it for polymerization of an aromatic polycarbonate may, for example, be mentioned.

In the present invention, the copper content in the diaryl carbonate is 1 ppm by weight or less. When the copper content is more than 1 ppm by weight, the color of the product aromatic polycarbonate is deteriorated, and the product is easily colored at a high temperature of 380 ° C. or higher, and the molecular weight is greatly reduced. Although the reason for this is not clear, it is assumed that the presence of copper acts catalytically on the coloring reaction and the molecular weight reduction reaction of the aromatic polycarbonate at high temperatures. The copper content in the diaryl carbonate is preferably 0.5 ppm by weight or less, more preferably 0.1 ppm by weight or less. The lower limit of the copper content is not particularly limited, and the copper content may be less than 0.001 weight ppm. However, even if the copper content is less than 0.001 weight ppm, the coloring of the aromatic polycarbonate at a high temperature is performed. And the effect of improving molecular weight reduction is small.

As a method for controlling the copper content within the above range, when producing the diaryl carbonate, no copper catalyst is used, or after producing the diaryl carbonate using the copper catalyst, the copper is subjected to a distillation operation, a washing operation, or the like. A method of reducing the content and the like can be mentioned. However, in the case of producing a diaryl carbonate without using any copper catalyst, it is preferable that other catalyst components that deteriorate the quality of the product polycarbonate are not contained in the diaryl carbonate.

In the present invention, the content of (p-phenoxyphenyl) (phenyl) carbonate in the diaryl carbonate is 1 ppm by weight or less. (P-phenoxyphenyl) (phenyl) carbonate content is 1 weight p
If it is higher than pm, the color of the product aromatic polycarbonate deteriorates, and it becomes easy to color at a high temperature of 380 ° C or higher. Although the reason for this is not clear, (p−
Phenoxyphenyl) (phenyl) carbonate itself,
Alternatively, it is presumed that a reaction product of (p-phenoxyphenyl) (phenyl) carbonate and an aromatic polycarbonate tends to be colored at a high temperature.

The content of (p-phenoxyphenyl) (phenyl) carbonate in the diaryl carbonate is preferably 0.5 ppm by weight or less, more preferably 0.1 ppm by weight or less.
It is not more than ppm by weight. The lower limit of the content of (p-phenoxyphenyl) (phenyl) carbonate is not particularly limited, and the content of (p-phenoxyphenyl) (phenyl) carbonate may be less than 0.01 ppm by weight. Even if the content of (p-phenoxyphenyl) (phenyl) carbonate is less than ppm, the effect of improving the coloring of the aromatic polycarbonate at a high temperature is small.

When producing an aromatic polycarbonate from an aromatic dihydroxy compound and a diaryl carbonate,
In order to industrially handle the diaryl carbonate preferably, the diaryl carbonate is usually used after being stored in a molten state. In the present invention, the diaryl carbonate is preferably stored in a stainless steel container in a molten state at a temperature of 80 to 190 ° C. in a nitrogen atmosphere. When the storage container is made of carbon steel, (p-phenoxyphenyl)
The amount of (phenyl) carbonate produced may increase.

The term “stainless steel” refers to the Stainless Steel Handbook No. 13
To 21 pages (published by Nikkan Kogyo Shimbun, 5th edition), stainless steels such as martensitic, ferritic, austenitic, ferritic and austenitic stainless steels usually containing 10 to 30% by weight of chromium as classified and classified. And Fe-based superalloys as shown in the table on page 547 of the Stainless Steel Handbook. As specific examples, SUS201,
SUS202, SUS304, SUS304L, SUS
316, SUS316L, SUS347, SUS40
5, SUS430, SUS403, SUS410, SU
S431, SUS440C, SUS630, Incoloy 800, Incoloy 801, Incoloy 802, Incoloy 807, Incoloy 901, LCN155, W54
5, V57, W545, D979, CG27, S590
And the like. A preferred example is SUS30
4, SUS304L, SUS316, SUS316L and the like, particularly preferably SUS304.

It is preferable that the liquid contact portion on the inner wall surface of the stainless steel container has been subjected to a washing treatment with phenol. When a stainless steel container washed with phenol is used, the amount of (p-phenoxyphenyl) (phenyl) carbonate produced can be particularly reduced. Although the reason for this is not clear, it is presumed that removal of oxygen adsorbed on the stainless steel surface with phenol prevents formation of (p-phenoxyphenyl) (phenyl) carbonate.

The storage is preferably carried out under a nitrogen atmosphere. When air is mixed in the storage container, the amount of (p-phenoxyphenyl) (phenyl) carbonate increases. The storage temperature is preferably in the range of 80 to 190 ° C., and if it is higher than 190 ° C., the amount of (p-phenoxyphenyl) (phenyl) carbonate formed tends to increase. When the temperature is lower than 80 ° C., it is not preferable because solidification occurs depending on the type of diaryl carbonate. A more preferred storage temperature range is from 85 to 160C, more preferably from 90 to 140C.

In the production of the aromatic polycarbonate in the present invention, the ratio of the aromatic dihydroxy compound and the diaryl carbonate to be used (the charge ratio) depends on the kind of the aromatic dihydroxy compound and the diaryl carbonate to be used, the polymerization temperature and other polymerization conditions. The diaryl carbonate is usually 0.9 to 2.5 mol, preferably 0.1 mol, per 1 mol of the aromatic dihydroxy compound.
It is used in a proportion of 95 to 2.0 mol, more preferably 0.98 to 1.5 mol. The number average molecular weight of the aromatic polycarbonate obtained by the method of the present invention is usually 5,000 to 1
00000, preferably 5000 to 300
00 range.

In the process for producing an aromatic polycarbonate of the present invention, the aromatic dihydroxy compound and the diaryl carbonate are heated under reduced pressure and / or inert gas flow in the presence or absence of a catalyst. This is a method in which polycondensation is performed by transesterification in a molten state, and the polymerization vessel is not particularly limited. For example, a stirred tank reactor, a thin film reactor, a centrifugal thin film evaporation reactor, a surface renewal type twin-screw kneading reactor, a twin-screw horizontal stirring reactor, a wet-wall reactor, and a perforated plate that polymerizes while falling freely A type reactor, a perforated plate type reactor with a wire that polymerizes while being dropped along a wire, or the like is used, and a polymerizer in which these are used alone or in combination is used. The polymerization can be performed either in a batch system or a continuous system. It is also preferable to use an extruder, a polymer mixer, or the like in combination with a polymerizer as a device for adding a stabilizer, an additive, and the like while the aromatic polycarbonate is in a molten state after the polymerization. The material of these polymerization vessels is not particularly limited, and is usually selected from stainless steel, nickel, glass lining and the like.

In the present invention, when the aromatic dihydroxy compound is reacted with the diaryl carbonate to produce an aromatic polycarbonate, the reaction temperature is usually selected from the range of 50 to 350 ° C., preferably 100 to 300 ° C. It is. As the reaction proceeds, an aromatic monohydroxy compound is generated. By removing this from the reaction system, the reaction rate can be increased. Therefore,
Introducing an inert gas such as nitrogen, argon, helium, carbon dioxide or a lower hydrocarbon gas which does not adversely affect the reaction, and removing the generated aromatic monohydroxy compound with these gases. Alternatively, a method of performing the reaction under reduced pressure is preferably used. The preferred reaction pressure also depends on the molecular weight, and is 10 mm
Hg to normal pressure is preferable.
Hg or less, especially 10 mmHg or less, preferably 2 mmHg
g or less.

The melt polycondensation reaction can be carried out without adding a catalyst. However, in order to increase the polymerization rate, the reaction is carried out in the presence of a catalyst if necessary. The polymerization catalyst is not particularly limited as long as it is used in this field, but hydroxides of alkali metals or alkaline earth metals such as lithium hydroxide, sodium hydroxide, potassium hydroxide and calcium hydroxide are used. Alkali metal salts, alkaline earth metal salts, quaternary ammonium salts of boron hydrides such as sodium borohydride and tetramethylammonium borohydride; alkalis such as lithium hydride, sodium hydride and calcium hydride Metal or alkaline earth metal hydrides;

Lithium methoxide, sodium ethoxy
Alkali metal such as
Alkoxides of alkaline earth metals; lithium phenoxy
, Sodium phenoxide, magnesium phenoxy
, LiO-Ar-OLi, NaO-Ar-ONa (A
r is an aryl group) or another alkali metal or alkaline earth
Allyloxides of the class of metals; lithium acetate, calcium acetate
Alkali metals such as sodium and sodium benzoate
Organic salts of alkaline earth metals; zinc oxide, zinc acetate, zinc oxide
Zinc compounds such as lead phenoxide; boron oxide, boron
Acid, sodium borate, trimethyl borate, triborate
Butyl, triphenyl borate, (R¹ R^TwoR^ThreeR^Four) N
B (R¹ R^TwoR^ThreeR^Four) Represented by ammonium volley
G, (R ¹ R^TwoR^ThreeR^Four) PB (R¹ R^TwoR^ThreeR^Four)
Phosphonium borates represented by the formula (R¹ , R^Two,
R^Three, R^FourIs as described in Chemical Formula 1. )
Elemental compounds;

Silicon compounds such as silicon oxide, sodium silicate, tetraalkylsilicon, tetraarylsilicon and diphenyl-ethyl-ethoxysilicon; germanium compounds such as germanium oxide, germanium tetrachloride, germanium ethoxide and germanium phenoxide A tin compound such as a tin compound or an organotin compound bonded to an alkoxy group or an aryloxy group such as tin oxide, dialkyltin oxide, dialkyltin carboxylate, tin acetate and ethyltin tributoxide; lead oxide, lead acetate, and carbonic acid Lead compounds such as lead, basic carbonate, alkoxide or aryloxide of lead and organic lead; onium compounds such as quaternary ammonium salts, quaternary phosphonium salts, and quaternary arsonium salts;

Compounds of antimony such as antimony oxide and antimony acetate; compounds of manganese such as manganese acetate, manganese carbonate and manganese borate; compounds of zirconium such as zirconium acetate, zirconium oxide and zirconium alkoxide or aryloxide and zirconium acetylacetone And the like. When a catalyst is used, these catalysts may be used alone or in combination of two or more. The amount of these catalysts used is usually 10 ^-8 to 1 based on 100 parts by weight of the raw material aromatic dihydroxy compound.
It is selected in the range of 10 parts by weight, preferably 10 ^-7 to 10 ^-1 parts by weight.

[0044]

BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, the present invention will be described in more detail with reference to embodiments of the present invention. -Moisture: Analyzed by Karl Fischer method. Copper content: Analyzed using ICP (high frequency inductively coupled plasma emission spectrometer; JY38PII manufactured by Seiko Instruments Inc.). -(P-phenoxyphenyl) (phenyl) carbonate content: analyzed by gas chromatography. Coloring: A solution obtained by dissolving 1 g of a sample in 7 ml of methylene chloride is placed in a cell having an optical path length of 1 cm, and the solution is measured by a spectrophotometer.
The absorbance at nm was measured and used as an index of coloring.

Ease of coloring at high temperature: Aromatic polycarbonate is heated at 380 ° C. for 30 minutes in a nitrogen atmosphere,
Evaluation was made based on the increase in the absorbance at 400 nm due to heating. -Number average molecular weight (Mn): Gel permeation chromatography (GPC) using tetrahydrofuran as a solvent Column: TSK-GEL, Tosoh Corporation
The molecular weight was measured by a production method, and determined using a reduced molecular weight calibration curve obtained by the following equation using standard monodispersed polystyrene. M _PC = 0.3591M _PS ^1.0388 (wherein, M _PC molecular weight of the aromatic polycarbonate, M _PS
Indicates the molecular weight of polystyrene. -Easiness of molecular weight reduction at high temperature: The aromatic polycarbonate was heated at 380 ° C for 30 minutes in a nitrogen atmosphere, and evaluated by the amount of decrease in the number average molecular weight due to heating.

[0046]

Example 1 After diphenyl carbonate was produced from dimethyl carbonate and phenol using diphenoxy copper as a catalyst, side cutting was performed in the gas phase of the second stage from the top of the column under the conditions of a pressure of 1596 Pa, a number of distillation stages of 5, and a reflux ratio of 3. Distilled and refined, placed in a SUS304 container under nitrogen atmosphere, 11
Stored at 0 ° C. for 100 hours. The diphenyl carbonate after storage had a water content of 0.1 ppm by weight, a copper content of 0.4 ppm by weight, and a (p-phenoxyphenyl) (phenyl) carbonate content of 0.1 ppm by weight. Using the diphenyl carbonate, an aromatic polycarbonate was produced by a process as shown in FIG.

The stirred tank type polymerization vessel 3 was operated in a batch manner, and the storage tank 10 and subsequent ones were continuously operated. Stirring tank type polymerization vessel 3 (capacity 200 liters), 17 (capacity 50 liters), 26
(Capacity 50 liters) are all equipped with stirring blades. Horizontal twin-screw stirring type polymerization vessel 35 (capacity 30 liters)
Has a biaxial stirring blade with L / D = 6 and a rotating diameter of 140 mm. The perforated-plate polymerization unit 42 with a wire has a pore size of 5
A SUS316L wire 44 having a diameter of 1 mm is provided vertically from the center of the hole.
Is hung down to the liquid reservoir at the bottom of the polymerization vessel, and the height at which it falls is 8 m.

The stirring tank type first polymerization vessel 3 has a reaction temperature of 180
° C, reaction pressure normal pressure, seal nitrogen gas flow rate 1 liter / h
r. 80 kg of fully degassed bisphenol A and the above-mentioned diphenyl carbonate (molar ratio of bisphenol A 1.10) were placed in a first polymerization vessel 3 of a stirred tank type.
7 mg of sodium hydroxide was charged and melt-mixed for 5 hours, and the molten polymer having a number-average molecular weight of 350 was transferred from the transfer pipe 7 to the storage tank 10 by pressure feeding.

The storage tank 10 is maintained at normal pressure and 180 ° C. The molten polymer transferred to the storage tank 10 was continuously supplied to the stirring tank type second polymerization device 17 at 10 kg / hr by the plunger pump 14. In the stirred tank type first polymerization vessel 3,
Before the molten polymer in the storage tank 10 runs out, a molten polymer having a number average molecular weight of 350 is produced in the same manner as described above, and transferred to the storage tank 10 again. Thereafter, similarly, a molten polymer having a number average molecular weight of 350 was produced batchwise in the first polymerization tank 3 of the stirring tank type, and was continuously supplied to the storage tank 10. Stirred tank type 2
The polymerization reactor 17 has a reaction temperature of 235 ° C. and a reaction pressure of 100 mm.
Under the condition of Hg, when the liquid volume of the molten polymer reaches 20 liters, the molten polymer having a number average molecular weight of 850 is continuously supplied to the third polymerization vessel 26 with a gear pump so as to keep the liquid volume constant at 20 liters. did. The stirring tank type third polymerization vessel 26 has a reaction temperature of 245 ° C. and a reaction pressure of 6 mmH.
g, and when the liquid volume of the molten polymer reaches 20 liters, the molten polymer having a number average molecular weight of 2,300 is continuously supplied to the horizontal twin-screw stirring type polymerizer 35 by a gear pump so as to keep the liquid volume at 20 liters. did.

In the horizontal twin-screw stirring type polymerization reactor 35, the reaction temperature is 270 ° C. and the reaction pressure is 67 Pa. When the liquid volume of the molten polymer reaches 10 liters, a wire is attached so that the liquid volume is kept constant at 10 liters. A molten polymer having a number average molecular weight of 6,100 was supplied to the perforated plate type polymerization vessel 42 by a gear pump. In the perforated-plate type polymerization device 42 with a wire, the reaction temperature is 260 ° C. and the reaction pressure is 53 Pa.
The number average molecular weight is 10,000 and 400 n from the outlet 51 through the transfer pipe 50 so as to maintain the liquid volume of 20 liters.
An aromatic polycarbonate having a good absorbance of 0.0027 m and a color of 0.0027 was extracted. After the obtained aromatic polycarbonate was heated at 380 ° C. for 30 minutes in a nitrogen atmosphere, the increase in absorbance was 0.0005, and the decrease in number average molecular weight was 3
It was hardly colored even at a high temperature, and the molecular weight was hardly reduced.

[0051]

Example 2 The same procedure as in Example 1 was carried out except that the storage conditions were 145 ° C. and 300 hours, and the water content of the produced, purified, and stored water was 0.1.
Example 1 was prepared using diphenyl carbonate having 1 ppm by weight, 0.4 ppm by weight of copper, and 0.3 ppm by weight of (p-phenoxyphenyl) (phenyl) carbonate.
An aromatic polycarbonate was produced in the same manner as described above to obtain a color-good aromatic polycarbonate having a number average molecular weight of 10,000 and absorbance of 0.0029 at 400 nm of 0.0029. The amount of increase in absorbance after heating the obtained aromatic polycarbonate at 380 ° C. for 30 minutes under a nitrogen atmosphere is 0.0006, the amount of decrease in number average molecular weight is 300, and coloring is difficult even at high temperatures.
Molecular weight reduction was unlikely to occur.

[0052]

Example 3 The same procedure as in Example 1 was carried out except that the storage conditions were 165 ° C. and 800 hours, and the water content of the produced, purified, and stored water was 0.1.
Example 1 was prepared using diphenyl carbonate having 1 ppm by weight, 0.4 ppm by weight of copper and 0.5 ppm by weight of (p-phenoxyphenyl) (phenyl) carbonate.
An aromatic polycarbonate was produced in the same manner as described above to obtain a color-good aromatic polycarbonate having a number average molecular weight of 10,000 and an absorbance of 0.0035 at 400 nm. The amount of increase in absorbance after heating the obtained aromatic polycarbonate at 380 ° C. for 30 minutes under a nitrogen atmosphere is 0.0008, the amount of decrease in number average molecular weight is 500, and it is difficult to discolor even at high temperature.
Molecular weight reduction was unlikely to occur.

[0053]

Embodiment 4 SUS3 whose inner wall surface has been washed with phenol
04, except that it was stored in a container made of 0.4, purified and stored in the same manner as in Example 3;
Ppm by weight, (p-phenoxyphenyl) (phenyl)
Using diphenyl carbonate having a carbonate content of 0.2 wt ppm, an aromatic polycarbonate was produced in the same manner as in Example 1 to obtain a good-colored aromatic polycarbonate having a number average molecular weight of 10,000 and an absorbance of 0.0028 at 400 nm of 0.0028. The amount of increase in absorbance after heating the obtained aromatic polycarbonate at 380 ° C. for 30 minutes in a nitrogen atmosphere is 0.0005, and the decrease in number average molecular weight is 300. Therefore, it is difficult to discolor even at a high temperature and the molecular weight is hardly reduced. Was.

[0054]

Example 5 The same procedure as in Example 1 was carried out except that the number of distillation stages was set to 3 and the reflux ratio was set to 0.8, the water content was 20 wt ppm, the copper content was 0.7 wt ppm, and the (p-phenoxy) Phenyl) (phenyl) carbonate content 0.1 wtp
Using diphenyl carbonate of pm, an aromatic polycarbonate was produced in the same manner as in Example 1, and the number average molecular weight was 1
An aromatic polycarbonate having a good color with an absorbance of 0000 and 400 nm of 0.0033 was obtained. The amount of increase in absorbance of the obtained aromatic polycarbonate after heating at 380 ° C. for 30 minutes in a nitrogen atmosphere is 0.0009, and the decrease in number average molecular weight is 700. Was.

[0055]

Example 6 The same procedure as in Example 1 was carried out except that the number of distillation stages was set to 3 and the reflux ratio was set to 0.1.
Aromatic polycarbonate was produced in the same manner as in Example 1 by using diphenyl carbonate having a weight ppm of copper, a copper content of 0.9 weight ppm, and a (p-phenoxyphenyl) (phenyl) carbonate content of 0.1 weight ppm, and a number average molecular weight was obtained. An aromatic polycarbonate having a good color with an absorbance of 10,000 and 400 nm of 0.0038 was obtained. The amount of increase in absorbance after heating the obtained aromatic polycarbonate at 380 ° C. for 30 minutes in a nitrogen atmosphere is 0.0013, and the decrease in number average molecular weight is 900, so that it is difficult to discolor even at a high temperature and the molecular weight is hardly reduced. Was.

[0056]

Example 7 The procedure of Example 1 was repeated except that the mixture was stored in an atmosphere containing 0.5% by volume of oxygen and 99.5% by volume of nitrogen. .4
Ppm by weight, (p-phenoxyphenyl) (phenyl)
Using diphenyl carbonate having a carbonate content of 0.9 wt ppm, an aromatic polycarbonate was produced in the same manner as in Example 1 to obtain a slightly colored aromatic polycarbonate having a number average molecular weight of 10,000 and an absorbance of 400 at 400 nm of 0.004. The amount of increase in absorbance after heating the obtained aromatic polycarbonate at 380 ° C. for 30 minutes under a nitrogen atmosphere is 0.002, and the decrease in number average molecular weight is 900, so that it is difficult to color at a high temperature and the molecular weight is hardly reduced. Was.

[0057]

Comparative Example 1 The procedure of Example 1 was repeated, except that distillation and purification were not carried out. The water content was 250 ppm by weight, the copper content was 1.5 ppm by weight, and the (p-phenoxyphenyl) (phenyl) carbonate content was 0.1 ppm by weight. Using diphenyl carbonate, an aromatic polycarbonate was produced in the same manner as in Example 1 to obtain a colored aromatic polycarbonate having a number average molecular weight of 10,000 and an absorbance of 0.0049 at 400 nm of 0.0049. The obtained aromatic polycarbonate was dried under nitrogen atmosphere.
The amount of increase in absorbance after heating at 80 ° C. for 30 minutes is 0.0
037, the amount of decrease in the number average molecular weight was 1,500, and it was easy to color at a high temperature, and the decrease in the molecular weight was large.

[0058]

COMPARATIVE EXAMPLE 2 Except for storage in an atmosphere of 2% by volume of oxygen and 98% by volume of nitrogen, the same procedure as in Example 1 was carried out to produce, purify and store 0.1% by weight of water and 0.4% by weight of copper.
m, an aromatic polycarbonate was produced in the same manner as in Example 1 using diphenyl carbonate having a content of 1.2 wt ppm of (p-phenoxyphenyl) (phenyl) carbonate and having a number-average molecular weight of 10,000 and an absorbance of 0.0059 at 400 nm of 0.0059. A colored aromatic polycarbonate was obtained. The obtained aromatic polycarbonate was dried under nitrogen atmosphere.
The amount of increase in absorbance after heating at 80 ° C. for 30 minutes is 0.0
044, the amount of decrease in the number average molecular weight was 1,400, and coloring was easy at high temperatures, and the decrease in molecular weight was large.

[0059]

According to the present invention, the color is good, and
Even at a high temperature of 80 ° C. or higher, a high-quality aromatic polycarbonate with little coloring and small molecular weight reduction can be produced by an industrially preferable method.

[Brief description of the drawings]

FIG. 1 is a flowchart showing an example of a process for producing an aromatic polycarbonate of the present invention.

[Explanation of symbols]

 1: Raw material supply port 2, 9, 19, 28, 36, 46: Vent port 3: Stirring tank type first polymerization device 4, 18, 27, 39: Stirring shaft 5, 11, 20, 29, 47: Molten polymer 6, 12, 21, 30, 37, 48: discharge port 7, 13, 15, 24, 33, 40, 50: transfer pipe 8, 16, 25, 34, 41: supply port 10: storage tank 14, 23, 32 , 38, 49: Transfer pump 17: Stirred tank type second polymerization unit 22, 31, 45: Gas supply port 26: Stirred tank type third polymerization unit 35: Horizontal biaxial stirring type polymerization unit 42: Perforated plate type with wire Polymerizer 43: Perforated plate 44: Wire 51: Product outlet

 ──────────────────────────────────────────────────続 き Continued on the front page F term (reference) 4J029 AA10 AB04 AC01 AE01 BB12A BB12B BB12C BB13A BB13B BB13C BD09A BD09B BD09C BE03 BE05A BE05B BF14A BF14B BH01 BH02 DA06 DB11 DB13 HC05A HC05 KD01 LA05

Claims (3)

[Claims] 1. A method for producing an aromatic polycarbonate which is polymerized in a molten state from an aromatic dihydroxy compound and a diaryl carbonate, wherein the diaryl carbonate has (a) a water content of 200 ppm by weight or less;
(B) The copper content is 1 ppm by weight or less, and (c) (p-
A method for producing an aromatic polycarbonate, wherein the content of phenoxyphenyl) (phenyl) carbonate is 1 ppm by weight or less. 2. A diaryl carbonate comprising: (a) a water content of not more than 200 ppm by weight; and (b) a copper content of 1%.
2. The aromatic polycarbonate according to claim 1, wherein the diaryl carbonate having a weight of not more than ppm is a diaryl carbonate stored in a molten state at a temperature of 80 to 190 [deg.] C. under a nitrogen atmosphere in a stainless steel container. Law. 3. The method for producing an aromatic polycarbonate according to claim 2, wherein the stainless steel container is a container in which the liquid contact portion on the inner wall surface has been subjected to a washing treatment with phenol.