Process for producing polycarbonate

Abstract: The object of the present invention is to obtain a polycarbonate having a high molecular weight, excellent in transparency and free from coloration from a dihydroxy compound and a diester of carbonic acid by transesterification. A polycarbonate is produced by transesterification from a dihydroxy compound such as 2,2-bis(4-hydroxyphenyl)propane and a diester of carbonic acid such as bisphenyl carbonate in the presence of a substance containing iron in an ammount of 50% by weight or less to contact the reactants. Examples of the substance include silicates such as glass; polyfluoroethylene; and metals and metal alloys which contain at least one element selected from the group consisting of Ni, Cr, Mo, Al, Cu, Zn, Co, Mn and C, and iron in an ammount of 50% by weight or less. A polycarbonate is produced by transesterification from a dihydroxy compound and a diester of carbonic acid in a reactor made of stainless steel and treated by electropolishing or acid pickling or buffed on a surface part thereof to contact the reactants. As the transesterification catalyst, (a) a nitrogen-containing, electron-donating compound and (b) a nitrogen-containing, electron-donating compound and an alkali metal compound or an alkaline earth metal compound are preferably used.

Description: The present invention relates to a process for producing a polycarbonate by transesterification, particularly a process for producing a polycarbonate, by which a polycarbonate which has little coloration and an enhanced molecular weight can be obtained. Polycarbonate is a general-purpose engineering thermoplastic excellent in mechanical properties, optical properties and heat resistance, and is used in extensive fields such as injection molding resin, sheet substitutive for window glass, etc. Polycarbonate has hitherto been produced by interfacial polycondensation or transesterification. Interfacial polycondensation method has widely been utilized in the general production of polycarbonates. However, it is disadvantageous in that toxic phosgene must be used and that the polymer produced by this method is colored when it was molded at high temperatures due to the residual chlorine ion present in the formed polycarbonate. In order to solve these problems, Japanese Patent Laid-Open No. 182336/1988 disclosed a process for producing a polycarbonate by using trichloromethyl chloroformate, which is liquid and a dimer of phosgene instead of toxic phosgene. However, dihydric phenols referred to therein as a starting material are limited to 9,9-bis(4-hydroxyphenyl)fluorenes which are special compounds as a dihydric phenol, so that the process disclosed therein cannot be thought to be a general-purpose process. On the other hand, in Angew. Chem. Vol. 99, Page 922 (1987) and German Patent DE 3440141, a process for producing a polycarbonate from 2,2-bis(4-hydroxyphenyl)propane by using triphosgene instead of toxic phosgene. In this process, however, phosgene is generated in the course of reaction. As an example of the methods using transesterification, US Patent No. 4,345,062 discloses a process which comprises synthesizing a prepolymer from diphenyl carbonate and an aromatic dihydroxy compound by heating under reduced pressure in the presence of a transesterification catalyst while distilling out formed phenol, and heating the obtained prepolymer to 270°C or above finally in a high vacuum while distilling out formed phenol to obtain a high molecular weight polycarbonate. This process is advantageous in that it uses no toxic phosgene, the removal of the residual chlorine ion is unnecessary, and the reaction can be carried out in a mode of melt-polycondensation. On the other hand, this process has been known to be disadvantageous that it generally requires a high reaction temperature of, for example, 270°C or above because polycarbonate increases its melt viscosity to a great extent as its molecular weight increases, unlike other engineering plastics, and that it necessitates a vacuum as high as 10 -2 Torr for distilling out formed phenol having a high boiling point. For these requirements in this process, the industrialization thereof is difficult from the standpoint of equipment. Further, the hue and physical properties of the obtained polycarbonate are adversely affected by the phenol remaining therein and due to the high reaction temperature. Moreover, transesterification method has not yet given a polycarbonate of high molecular weight. In spite of the above disadvantages, many studies have been made on the transesterification method, because the method is an industrially economical process which can give a polycarbonate by melt-polycondensation. Particularly, it has been suggested that the material of the reaction vessel used exerts an influence to the coloration of the product. Namely, in Japanese Patent Laid-Open No. 142025/1980, it is suggested that, when stainless steel is used as the material constructing the reactor in the preparation of polycarbonate by transesterification method, the formed polycarbonate is apt to be colored and a polymer of high molecular weight is difficult to obtain, so that the production of a polymer excellent in both properties and color cannot be achieved. Further, the inventors of the present invention found that when a carbon steel or a stainless steel was used as such as the material of the reactor in the preparation of polycarbonate by transesterification method using a transesterification catalyst, the molecular weight of polycarbonate could not be enhanced enough with the reproducibility thereof being poor and the obtained polycarbonate was significantly colored. To overcome these problems, it has been proposed in U.S. Patent No. 4383092 that the coloration of the product is inhibited by using tantalum, nickel or chromium as the material of the reactor. However, a reactor made of only these metals is too expensive to be practical in this respect. In Japanese Patent Laid-Open No. 72327/1992, published on March 6, 1992, the use of a reactor made of a material comprising Cu and/or Ni in an amount of 85% by weight or above is proposed. Further, in Japanese Patent Laid-Open No. 124934/1990, the use of a reactor made of glass and a stirrer made of nickel is mentioned and in Japanese Patent Laid-Open No. 153923/1990, the use of glass, nickel, tantalum, chromium or polyfluoroethylene as the material of the reactor is mentioned. With the aim of overcoming the above-mentioned faults of transesterification method, a variety of catalysts have also been studied (Japanese Patent Laid-Open No. 142025/1980, for example). However, none of these catalysts can simultaneously fulfil the requirements concerning the properties and color of polycarbonate. Accordingly, the object of the present invention is to provide an industrial process for producing a polycarbonate having high molecular weight and which is free from coloration with a high efficiency. The inventors of the present invention have made intensive studies on the molecular weight of the polycarbonate and the coloration thereof in which the polycarbonate prepared by the transesterification method of the prior art were problematic. As a result, they have found that a polycarbonate having an enhanced molecular weight and excellent in transparency can be obtained by a process for producing a polycarbonate by transesterification, which comprises reacting a dihydroxyl compound with a diester of carbonic acid in a reactor at least the surface area of which being brought into contact with the reactants, is made of a metal alloy containing iron in an amount of from 20% to 50% by weight. The metal alloy which contains iron in an amount of from 20% to 50% by weight may further contain Cr and/or Co in an amount of 50% by weight or above or Al and/or Mn in an amount of 50% by weight or above. The metal alloy preferably contains iron in an amount of from 20% to 40% by weight. The metal alloy which contains iron in an amount of from 20% to 40% by weight may further contain Ni and/or Cr in an amount of 60% by weight or above, Ni and/or C in an amount of 60% by weight or above, Ni and/or Mo in an amount of 60% by weight or above, Ni and/or Al in an amount of 60% by weight or above, Ni and/or Cu in an amount of 60% by weight or above, Cu and/or Al in an amount of 60% by weight or above or Cu and/or Zn in an amount of 60% by weight or above. Preferably, the transesterification is carried out in the presence of (a) a nitrogen-containing, electron-donating compound or (b) a nitrogen-containing, electron-donating compound and an alkali metal compound or an alkaline earth metal compound. In the present invention, a variety of compounds can be used as the dihydroxy compound. For example, bis(hydroxyaryl)alkanes, bis(hydroxyaryl)arenes, bis(hydroxyaryl)cycloalkanes, dihydroxydiaryl ethers, dihydroxydiaryl sulfides, dihydroxydiaryl sulfoxides and dihydroxydiaryl sulfones, can be used. Among these compounds, preferable dihydroxy compounds are those represented by the following general formulas (I), (II), (III): wherein R 1 , R 2 , R 3 , R 4 , R 5 and R 6 , which may be the same or different, each represent a hydrogen atom, an alkyl group, a cycloalkyl group, an aralkyl group or an aryl group; X 1 , X 2 , Y 1 , Y 2 , Y 3 , Z 1 and Z 2 , which may be the same or different, each represent a halogen atom, an alkoxy group, an alkyl group, a cycloalkyl group, an aralkyl group or an aryl group; l, m, n, p, q, r and s each represent an integer of 0-4; and t represents an integer of 2-10. Among these, those compounds represented by the following general formulae (IV), (V), (VI) and (VII) are especially preferred: wherein R 7 , R 8 , R 9 , R 10 and R 11 each represent a hydrogen atom, a straight-chain or branched alkyl group having 1 to 8 carbon atoms or a phenyl group; X 3 represents a halogen atom; u is 0 to 4; and v is 1 to 4. Examples of the alkyl group include straight-chain or branched alkyl groups such as methyl group, ethyl group, n-propyl group, isopropyl group, n-butyl group, isobutyl group, t-butyl group, n-pentyl group, isopentyl group, neopentyl group, hexyl group, heptyl group, octyl group, 2-ethylhexyl group, decyl group, undecyl group and dodecyl group, among which preferable alkyl groups are straight-chain or branched alkyl groups having 1 to 8 carbon atoms. Examples of the cycloalkyl group include cyclopropyl group, cyclopentyl group, cyclohexyl group, cycloheptyl group and cyclooctyl group. Examples of the aralkyl group include benzyl group, phenethyl group and benzhydryl group. Examples of the aryl group include phenyl group, naphthyl group and anthryl group, among which a preferable aryl group is phenyl group. The halogen atom includes fluorine atom, chlorine atom, bromine atom and iodine atom. The alkoxy group includes methoxy group, ethoxy group, n-propoxy group, isopropoxy group, n-butoxy group, isobutoxy group, pentyloxy group and hexyloxy group. The alkyl group, the cycloalkyl group, the aryl group and the aralkyl group may have one or more substituents inert under the conditions of the transesterification reaction. Examples of such substituent include a halogen atom, an alkoxy group, an aryloxy group, an aralkyloxy group, an alkylthio group, a cyano group and a nitro group. As the substituents R 1 to R 6 , a hydrogen atom, an alkyl group (particularly those having 1 to 8 carbon atoms) and an aryl group (particularly a phenyl group) are preferred. As the substituents X 1 , X 2 , Y 1 , Y 2 , Y 3 , Z 1 and Z 2 , an alkyl group (particularly those having 1 to 8 carbon atoms), an aryl group (particularly a phenyl group) and a halogen atom are preferred. Preferable examples of the dihydroxy compound include 2,2-bis(4-hydroxyphenyl)propane, 2,2-bis(4-hydroxyphenyl)butane, 2,2-bis(4-hydroxyphenyl)-4-methylpentane, 2,2-bis(4-hydroxyphenyl)octane, 4,4'-dihydroxy-2,2,2-triphenylethane, 2,2-bis(3,5-dibromo-4-hydroxyphenyl)propane, 2,2-bis(4-hydroxy-3-methylphenyl)propane, 2,2-bis(4-hydroxy-3-isopropylphenyl)propane, 2,2-bis(4-hydroxy-3-sec-butylphenyl)propane, 2,2-bis(3,5-dimethyl-4-hydroxyphenyl)propane, 2,2-bis(4-hydroxy-3-tert-butylphenyl)propane, 1,1'-bis(4-hydroxyphenyl)-p-diisopropylbenzene, 1,1'-bis(4-hydroxyphenyl)-m-diisopropylbenzene and 1,1-bis(4-hydroxyphenyl)cyclohexane. These dihydroxy compounds can be used either alone or in combination of two or more members among them for the production of a copolycarbonate. Examples of the diester of carbonic acid include bisaryl carbonates such as diphenyl carbonate, bis(2,4-dichlorophenyl) carbonate, bis(2,4,6-trichlorophenyl) carbonate, bis(2-cyanophenyl) carbonate, bis(o-nitrophenyl) carbonate, ditolyl carbonate, m-cresyl carbonate, dinaphthyl carbonate and bis(diphenyl) carbonate; dicycloalkyl carbonates such as dicyclohexyl carbonate; and dialkyl carbonates such as dimethyl carbonate and diethyl carbonate. Among these, bisaryl carbonates are preferable, and diphenyl carbonate is particularly preferred. The diester of carbonic acid is used in an amount equimolar to that of the dihydroxyl compound present in the reaction system. Generally, 1 mol of a carbonate compound must be reacted with 1 mol of a dihydroxyl compound in order to form a high-molecular weight polycarbonate. When a bisaryl carbonate is used as the diester of carbonic acid, two molecules of a monohydroxyl compound are liberated by the above-mentioned reaction. According to the present invention, this monohydroxyl compound is distilled out of the reaction system. However, in the industrial process of the prior art, an excess of a diester of carbonic acid is reacted with a dihydroxyl compound. Therefore, the amount of the diester of carbonic acid which is used as a starting material is usually 0.90 to 1.50 mol, preferably 0.95 to 1.25 mol, and still preferably about 1.00 to 1.10 mol, per mole of the dihydroxy compound as other starting material. The process for producing a polycarbonate by transesterification, which comprises reacting a dihydroxyl compound with a diester of carbonic acid in a reactor, at least the surface area of which being brought into contact with the reactants, is made of a metal alloy containing iron in an amount of from 20% to 50% by weight will be described in detail. According to the present invention the metal alloy may be further classified into two groups, i.e., one containing iron in ammount of from 20% to 50% by weight and one containing iron in ammount of from 20% to 40% by weight. The metal alloy used in the present invention includes those which contain iron in ammount of from 20 to 50% by weight and further contain Cr and/or Co in an amount of 50% by weight or above or Al and/or Mn in an amount of 50% by weight or above. Namely, the metal alloy used in the present invention includes, for example, one which contains iron in ammount of from 20 to 50% by weight, and Cr in an amount of 50% by weight or above; one which contains iron in ammount of from 20 to 50% by weight, and Co in an amount of 50% by weight or above; and one which contains iron in ammount of from 20 to 50% by weight, and Cu and Cr in a total amount thereof of 50% by weight or above. The metal alloy used in the present invention includes those which contain iron in ammount of from 20 to 40% by weight and further contain Ni and/or Cr in an amount of 60% by weight or above, Ni and/or C in an amount of 60% by weight or above, Ni and/or Mo in an amount of 60% by weight or above, Ni and/or Al in an amount of 60% by weight or above, Ni and/or Cu in an amount of 60% by weight or above, Cu and/or Al in an amount of 60% by weight or above or Cu and/or Zn in an amount of 60% by weight or above. According to the present invention, a colorless transparent polycarbonate having a high molecular weight is obtained when a metal alloy is used which contains iron in ammount of 50% by weight or less and further contains Cr and/or Co in an amount of 50% by weight or above or Al and/or Mn in an amount of 50% by weight or above. The content of the total of Cr and Co, or, Al and Mn in a metal alloy is preferably 60% by weight or above, still preferably 70% by weight or above. As the examples of other metallic and nonmetallic components which the alloys can contain, e.g. W, Mo, Ti, Zr, Mn, Al, Cu, Fe, Ni, Sn, Zn, Mg, Si, C, P and S can be mentioned. According to the present invention, a colorless transparent polycarbonate having a high molecular weight is obtained when a metal alloy is used which contains iron in ammount of from 20 to 40% by weight and further contains Ni and/or Cr in an amount of 60% by weight or above, Ni and/or C in an amount of 60% by weight or above, Ni and/or Mo in an amount of 60% by weight or above, Ni and/or Al in an amount of 60% by weight or above, Ni and/or Cu in an amount of 60% by weight or above, Cu and/or Al in an amount of 60% by weight or above or Cu and/or Zn in an amount of 60% by weight or above. A colorless transparent polycarbonate having a high molecular weight is also obtained when the metal alloy, which contains iron in ammount of from 20 to 40% by weight or less, Ni and/or Cr in an amount of 60% by weight or above and Mo, is selected. In these alloys, e.g. Fe, Pb, Zn, Ti and V may be incorporated as other components. If the content of above-described elements is lower than 60% by weight, the formation of high molecular weight product is obstructed, or the coloration of resin is accelerated. Cases where these "other components" are present in a minute quantity are also included in the scope of the present invention. Further, said "other components" are not limited to the above-mentioned ones. The reactor to be used in the method of the present invention is not particularly critical, so far as it is made of the above-described metal alloy at least in the positions coming into contact with the reactants. That is, a reactor for the transesterification reaction which has a surface.area made of the metal alloy which the reactants are brought into contact with can be used in the method of the present invention. The above-described surface layer is made, for example, by plating with metal alloy on a reactor made of, e.g., stainless steel or carbon steel. The term "plating" used herein inclusively means electroplating, chemical plating and vacuum metallizing generally, among which the industrially preferable methods are electroplating (electrolytic plating) and chemical plating (electroless plating). As the plating metal, the metal alloys described above according to the substance can be used. As the body material, carbon steel and stainless steel which are inexpensive and usable at high temperatures (300 to 350°C) are usually preferable. The method of the present invention can further be conducted by additionelly reacting the reactants in the presence of an additive of which at least surface is made of a substance selected from a silicate, ceramics, polyfluoroethylene, metals other than iron, such as Ni, Cr, Mo, Al, Cu, Zn, Co, Mn or Ta; carbon; metal alloys containing iron in an ammount of 50% by weight or less, such as a metal alloy containing iron in an amount of from 20% to 50% by weight, a metal alloy which contains iron in an amount of from 20% to 50% by weight and further contains Cr and/or Co in an amount of 50% by weight or above or Al and/or Mn in an amount of 50% by weight or above, a metal alloy containing iron in an amount of from 20% to 40% by weight, a metal alloy which contains iron in an amount of from 20% to 40% by weight and further contains Ni and/or Cr in an amount of 60% by weight or above, Ni and/or C in an amount of 60% by weight or above, Ni and/or Mo in an amount of 60% by weight or above, Ni and/or Al in an amount of 60% by weight or above, Ni and/or Cu in an amount of 60% by weight or above, Cu and/or Al in an amount of 60% by weight or above or Cu and/or Zn in an amount of 60% by weight or above, a metal alloy containing iron in an amount of 20% by weight or less, a metal alloy which contains iron in an amount of 20% by weight or less and further contains Ni and/or Cr in an amount of 60% by weight or above, Ni and/or C in an amount of 60% by weight or above, Ni and/or Mo in an amount of 60% by weight or above, Ni and/or Al in an amount of 60% by weight or above, Ni and/or Cu in an amount of 60% by weight or above, Cu and/or Al in an amount of 60% by weight or above, Cu and/or Zn in an amount of 60% by weight or above, Cr and/or Co in an amount of 50% by weight or above or Al and/or Mn in an amount of 50% by weight or above, a metal alloy comprising Cu and/or Ni in an amount of from 60% to less than 85% by weight and Fe in an amount of 40% by weight or less, and a metal alloy comprising Cu and Zn in an amount of from 60% to 99.5% by weight and Fe in an amount of 40% by weight or less. The shape and morphology of the additive is not critical. Additives made of the substance and having a form of powder, granule, rod, plate, cylinder, mass or ribbon can be used. for example. Among these forms, powdery form is particularly preferred. Additives having a surface layer of the above-described substance are also used. The amount of the additive is about 1 ppm to about 1% by weight, preferably 5 ppm to 5,000 ppm, and still preferably about 20 ppm to about 1,000 ppm, based on the total weight of the reactants. If its amount is smaller than 1 ppm, the formed polycarbonate has a low molecular weight and is readily colored. If its amount is larger than 1% by weight, the procedure for separating the additive is complicated. In the process of the present invention, the reaction is carried out usually in the presence of a transesterification catalyst. As typical examples of the transesterification catalyst, the following catalysts (A), (B), (C), (D) and (E) can be mentioned. (A) Metal-containing catalysts The metal-containing catalysts include, for example, metal borohydrides such as lithium borohydride, sodium borohydride, potassium borohydride, rubidium borohydride, cesium borohydride, beryllium borohydride, magnesium borohydride, calcium borohydride, strontium borohydride, barium borohydride, aluminum borohydride, titanium borohydride, tin borohydride and germanium borohydride; metal tetraphenoxides such as tetraphenoxylithium, tetraphenoxysodium, tetraphenoxypotassium, tetraphenoxyrubidium and tetraphenoxycesium; sodium thiosulfate; metal oxides such as beryllium oxide, magnesium oxide, antimony trioxide and tin (IV) oxide; dibutyltin oxide; metal hydroxides such as beryllium hydroxide, magnesium hydroxide and germanium hydroxide; metal acetates such as beryllium acetate, zinc acetate, magnesium acetate and tin (IV) acetate; metal carbonates such as lithium carbonate, sodium carbonate, potassium carbonate, beryllium carbonate, magnesium carbonate, tin (IV) carbonate and germanium carbonate; metal nitrates such as tin (IV) nitrate and germanium nitrate; metal phenylacetates such as zinc phenylacetate, lead phenylacetate and tin phenylacetate; and bismuth trimethylcarboxylate. (B) Catalysts belonging to nitrogen-containing, electron-donating compounds including e.g. primary amines, secondary amines, tertiary amines and nitrogen-containing heterocyclic compounds. Examples of such catalysts include N,N-dimethyl-4-aminopyridine (represented by 4-dimethylaminopyridine, hereinafter), N,N-diethyl-4-aminopyridine, 4-pyrrolidinopyridine, pyridine, 4-aminopyridine, 2-aminopyridine, 2-hydroxypyridine, 4-hydroxypyridine, 2-methoxypyridine, 4-methoxypyridine, picoline, pyrimidine, 2-dimethylaminoimidazole, 2-methoxyimidazole, 2-mercaptoimidazole, aminoquinoline, imidazole, 2-methylimidazole, 4-methylimidazole, pyrazole, benzimidazole, N,N-dimethylaniline, pyrrolidine, morphaline, N-methylmorpholine, piperidine, piperazine, 1,4-diazabicyclo[2.2.2]octane (DABCO), 1,8-diazabicyclo[5.4.0]-7-undecene (DBU) and 1,5-diazabicyclo[4.3.0]-5-nonene (DBN). (C) Salts formed between the above-mentioned nitrogen-containing electron-donating compounds and acids such as carbonic acid, acetic acid, formic acid, nitric acid, nitrous acid, oxalic acid, borofluoric acid and hydrofluoric acid. (D) Catalysts belonging to electron-donating phosphorus compounds Examples of such catalysts include triethylphosphine, tri-n-propylphosphine, triisopropylphosphine, tri-n-butylphosphine, triphenylphosphine, tri-o-dimethoxyphenylphosphine, tri-p-tolylphosphine, tri-o-tolylphosphine, tributyl phosphite, triphenyl phosphite, tri-p-tolyl phosphite and tri-o-tolyl phosphite. (E) Catalysts belonging to borane complexes Examples of such catalysts include complexes formed between borane and ammonia, dimethylamine, trimethylamine, triethylamine, t-butylamine, dimethylaniline, pyridine, dimethylaminopyridine, morpholine, piperazine, pyrrole, tetrahydrofuran, dimethyl sulfide, tri-n-butylphosphine, triphenylphosphine and triphenyl phosphite. These transesterification catalysts may be used either alone or in the form of a mixture of two or more members among them. Among these transesterification catalysts, preferable are (a) a nitrogen-containing, electron-donating compound and (b) a mixture of a nitrogen-containing, electron-donating compound and an alkali metal compound or an alkaline earth metal compound. Among them, 2-methylimidazole, 4-dimethylaminopyridine and a mixture of 4-dimethylaminopyridine and potassium acetate are more preferable. The alkali metal compound and alkaline earth metal compound include e.g. oxides, hydroxides, organic acid salts, carbonates, hydrogencarbonates, thiosulfates and borohydrides of alkali metals and alkaline earth metals. As the examples of such compounds, the compounds which have been mentioned in paragraph (A) and fulfil the conditions of this paragraph can be referred to. The amount of the transesterification catalyst may be any so long as the polycondensation reaction is not disturbed by its use. For example, the catalyst is used in an amount of 10 -7 to 10 -1 mol, preferably about 10 -5 to 10 -1 mol, more preferably about 10 -5 to 10 -2 mol, most preferably about 10 -4 to 10 -2 mol, per mole of the dihydroxy compound. If the amount of the catalyst is smaller than 10 -7 mol per mole of the dihydroxy compound, the rate of polymerization reaction forming polycarbonate is low because the catalytic activity is low. If the amount of the catalyst is larger than 10 -1 mol, the catalyst remains in the formed polycarbonate to deteriorate the properties of the polycarbonate. The transesterification reaction is carried out usually at a temperature of about 100°C to 300°C, preferably at about 130°C to 280°C. If the reaction temperature is lower than 100°C, the reaction velocity is low. If the reaction temperature is higher than 300°C, side reactions readily take place. It is also possible to carry out the reaction according to the conventional procedure adopted in melt-polycondensation reactions, i.e. by carrying out the early stage of the reaction at 100°C to 250°C, preferably at about 130°C to 230°C, and thereafter elevating the temperature while reducing the pressure, and finally carrying out the reaction at about 250°C to 300°C. Preferably, the pressure at the completing of the reaction is 0.3 Torr or below. The polycarbonate obtained according to the process of the present invention has a high molecular weight and is free from coloration and excellent in mechanical and electrical properties, heat resistance, transparency and light resistance. Thus, it can be used as electronic and electric parts, mechanical parts, structural materials, films, sheets, containers, etc. According to the process of the present invention, there can be obtained a colorless, transparent polycarbonate which is free from coloration in spite of its high molecular weight. The present invention will now be described by referring to the following Examples, though the present invention is not limited to them. (Example) In Examples and Comparetive Examples, the viscosity-average molecular weight ( M v) of a polymer was determined by measuring the intrinsic viscosity [η] of a methylene chloride solution of a polycarbonate sample at 20°C with a Ubbellohde viscometer, followed by calculation according to the following equation: [η] = 1.11 × 10 -4 ( M v) 0.82 . The hue of a polymer was evaluated by determining the absorbances of a 10% solution of a polycarbonate sample in methylene chloride at wavelengths of 380 nm and 580 nm with an UV spectrophotometer and calculating the difference between the absorbances. A greater value means a higher extent coloration. Comparative Example 1 22.8 g (0.1 mol) of 2,2-bis(4-hydroxyphenyl)propane, 0.0164 g (2 × 10 -4 mol) of 2-methylimidazole and 21.9 g (0.1023 mol) of bisphenyl carbonate were fed into a reaction vessel made of Hastelloy B (comprising 64wt.% of Ni, 28wt.% of Mo, 5wt.% of Fe, 1.0wt.% of Cr, 0.8wt.% of Mn and 0.7wt.% of Si). The contents were stirred at 180°C in a nitrogen gas atmosphere for 1 hour. Then, the reaction system was heated while reducing the pressure gradually and reached at 270°C and 0.1 Torr finally. The contents were polycondensed at the condition (270°C and 0.1 Torr) for 2 hours, while distilling off the formed phenol. Thus, a colorless transparent polycarbonate was obtained. The viscosity-average molecular weight ( M v) of the polycarbonate was 29,000, while the hue (A 380 - A 580 ) thereof was 0.10. Comparative Example 2 A polycarbonate was prepared in the same manner as that of Comparative Example 1 except that a reaction vessel made of Hastelloy C (comprising 57wt.% of Ni, 17wt.% of Mo, 16.5wt.% of Cr, 5wt.% of Fe, 2.5wt.% of Co, 0.8wt.% of Mn and 0.7wt.% of Si) and 0.0061 g (5 × 10 -5 mol) of 4-dimethylaminopyridine, as a transesterification catalyst instead of the 2-methylimidazole, were used. The viscosity-average molecular weight ( M v) of the polycarbonate was 33,000, while the hue (A 380 - A 580 ) thereof was 0.07. Example 1 A polycarbonate was prepared in the same manner as that of Comparative Example 1 except that a reaction vessel made of Incoloy 825 (comprising 42wt.% of Ni, 21.5wt.% of Cr, 3wt.% of Mo, 2.2wt.% of Cu and 30wt.% of Fe) was used and that 0.0061 g (5 × 10 -5 mol) of 4-dimethylaminopyridine and 0.00049 g (5 × 10 -6 mol) of potassium acetate were used as transesterification catalysts instead of the 2-methylimidazole. The viscosity-average molecular weight ( M v) of the polycarbonate is 32,000, while the hue (A 380 - A 580 ) thereof is 0.10. Example 2 A polycarbonate is prepared in the same manner as that of Example 1 except that a reaction vessel made of Incoloy 800 (comprising 32.5wt.% of Ni, 21wt.% of Cr and 46.5wt.% of Fe) is used. The viscosity-average molecular weight ( M v) of the polycarbonate is 29,000, while the hue (A 380 - A 580 ) thereof is 0.11. Comparative Example 3 22.8 g (0.1 mol) of 2,2-bis(4-hydroxyphenyl)propane, 0.0122 g (1 × 10 -4 mol) of 4-dimethylaminopyridine and 21.9 g (0.1023 mol) of bisphenyl carbonate were fed into a reaction vessel made of stainless steel (SUS 316; comprising 67wt.% of Fe, 18wt.% of Cr, 12wt.% of Ni, 2.5wt.% of Mo and 0.06wt.% of C). The contents were stirred at 180°C in a nitrogen gas atmosphere for 1 hour. Then, the reaction system was heated while reducing the pressure gradually and reached at 270°C and 0.1 Torr finally. The contents were polycondensed at the condition (270°C and 0.1 Torr) for 2 hours, while distilling off the formed phenol. Thus, a polycarbonate was obtained. The viscosity-average molecular weight ( M v) of the polycarbonate was 18,000, while the hue (A 380 - A 580 ) thereof was 0.319. Comparative Example 4 A polycarbonate was prepared in the same manner as that of Comparative Example 3 except that a reaction vessel made of stainless steel (SUS 304; comprising 74wt.% of Fe, 18wt.% of Cr, 8wt.% of Ni and 0.06wt.% of C) was used. The viscosity-average molecular weight ( M v) of the polycarbonate was 21,400, while the hue (A 380 - A 580 ) thereof was 0.276. Comparative Example 5 A polycarbonate was prepared in the same manner as that of Example 2 except that a reaction vessel made of carbon steel (SS-41) was used. The viscosity-average molecular weight ( M v) of the polycarbonate was 14,300, while the hue (A 380 - A 580 ) thereof was 0.283. Comparative Example 6 A polycarbonate was prepared in the same manner as that of Comparative Example 1 except that a reaction vessel made of stainless steel (SUS 316) was used. The viscosity-average molecular weight ( M v) of the polycarbonate was 18,000, while the hue (A 380 - A 580 ) thereof was 0.319. Comparative Example 7 A polycarbonate was prepared in the same manner as that of Comparative Example 1 except that a reaction vessel made of stainless steel (SUS 304) was used. The viscosity-average molecular weight ( M v) of the polycarbonate was 17,000, while the hue (A 380 - A 580 ) thereof was 0.354. Comparative Example 8 A polycarbonate was prepared in the same manner as that of Comparative Example 1 except that a reaction vessel made of carbon steel (SS-41) was used. The viscosity-average molecular weight ( M v) of the polycarbonate was 14,300, while the hue (A 380 - A 580 ) thereof was 0.429. Comparative Example 9 A polycarbonate was prepared in the same manner as that of Example 1 except that a reaction vessel made of stainless steel (SUS 316) was used. The viscosity-average molecular weight ( M v) of the polycarbonate was 21,000, while the hue (A 380 - A 580 ) thereof was 0.38. Comparative Example 10 A polycarbonate was prepared in the same manner as that of Example 1 except that a reaction vessel made of stainless steel (SUS 304) was used. The viscosity-average molecular weight ( M v) of the polycarbonate was 20,000, while the hue (A 380 - A 580 ) thereof was 0.40. Comparative Example 11 A polycarbonate was prepared in the same manner as that of Example 1 except that a reaction vessel made of carbon steel (SS-41) was used. The viscosity-average molecular weight ( M v) of the polycarbonate was 17,000, while the hue (A 380 - A 580 ) thereof was 0.50.

Claims: A process for producing a polycarbonate by transesterification, which comprises reacting a dihydroxyl compound with a diester of carbonic acid in a reactor, at least the surface area of which being brought into contact with the reactants, is made of a metal alloy containing iron in an amount of from 20% to 50% by weight. The process according to claim 1, wherein the metal alloy further contains Cr and/or Co in an amount of 50% by weight or above or Al and/or Mn in an amount of 50% by weight or above. The process according to claim 1, wherein the metal alloy contains iron in an amount of from 20% to 40% by weight. The process according to claim 3, wherein the metal alloy further contains Ni and/or Cr in an amount of 60% by weight or above, Ni and/or C in an amount of 60% by weight or above, Ni and/or Mo in an amount of 60% by weight or above, Ni and/or Al in an amount of 60% by weight or above, Ni and/or Cu in an amount of 60% by weight or above, Cu and/or Al in an amount of 60% by weight or above, or Cu and/or Zn in an amount of 60% by weight or above. The process according to claim 1, wherein the transesterification is carried out in the presence of (a) a nitrogen-containing, electron-donating compound or (b) a nitrogen-containing, electron-donating compound and an alkali metal compound or an alkaline earth metal compound.

Inventors: FUKUDA YUTAKA, KANNO TATSUYA, KUWANA TAKAAKI, OKANO YOSHIMICHI, OSHINO YASUHIRO, YAMATO TSUTOMU, FUKUDA, YUTAKA, KANNO, TATSUYA, KUWANA, TAKAAKI, OKANO, YOSHIMICHI, OSHINO, YASUHIRO, YAMATO, TSUTOMU
Applicants: DAICEL CHEM, DAICEL CHEMICAL INDUSTRIES, LTD.
Application year: 1992
Main classification: C08G64
IPC codes: C08G64