JP2007182477A - Polyester resin, polyester resin composition comprising the same and its application - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a phosphorus-containing polyester resin that can be used for solving the problems, of conventional techniques, of formation of aldehydes such as acetaldehyde or cyclic oligomers on molding, deterioration in transparency of molded items, or the like and has a decreased content of metal atoms eluting from a polymerization vessel by deactivating actions of a polycondensation catalyst used in the manufacture of the polyester, a polyester resin composition efficiently producing a blow molded item or the like that is excellent in transparency and flavor retention, is free from problems such as deterioration in transparency caused by mold stains on continuous molding and exhibits excellent dimensional stability under heat, and a molded item composed of the same. <P>SOLUTION: The polyester resin is mainly composed of an aromatic dicarboxylic acid component and a glycol component and contains 100-10,000 ppm, in terms of the phosphorus atom, of a phosphorous compound, and has a Cr atom content (Cr) and an Fe atom content (Fe) satisfying the expression A: Cr≤10 ppm and the expression B: Fe≤30 ppm, respectively. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

  The present invention relates to a polyester resin that can be used for deactivating the action of a polycondensation catalyst used during the production of polyester and suppressing the formation of aldehydes such as acetaldehyde and cyclic oligomers during molding, and a polyester resin comprising the same. The present invention relates to a composition and its use.

  Polyester whose main repeating unit is ethylene terephthalate (hereinafter sometimes abbreviated as PET or PET resin) is a carbonated beverage due to its excellent properties such as transparency, mechanical strength, heat resistance and gas barrier properties. It is adopted as a material for containers such as juice and mineral water, and its spread is remarkable. Mass production by a continuous polymerization method is carried out in a factory. In these applications, beverages that have been sterilized at high temperatures are hot-filled in polyester bottles, or sterilized at high temperatures after filling beverages. However, ordinary polyester bottles shrink during such hot-filling treatments. Deformation occurs and becomes a problem. As methods for improving the heat resistance of polyester bottles, methods have been proposed in which the bottle cap is heat treated to increase the degree of crystallinity and the stretched bottle is heat-set. In particular, when the crystallization of the plug portion is insufficient or the variation in crystallinity is large, the sealing performance with the cap is deteriorated, and the contents may leak.

  Specifically, in the case of beverages that require hot filling, such as fruit juice beverages, oolong tea, and mineral water, a method of crystallizing by heat treatment of the preform or the bottle stopper portion of the bottle (for example, Patent Documents 1 and 2) are common. Such a method, that is, a method of improving the heat resistance by heat-treating the plug portion and the shoulder portion, the time and temperature for the crystallization treatment greatly affect the productivity, and can be processed at a low temperature in a short time. It is preferable that the conversion rate is PET. On the other hand, the body portion is required to be transparent even if heat treatment is performed at the time of molding so as not to deteriorate the color tone of the contents of the bottle, and the mouthpiece portion and the body portion must have contradictory characteristics.

  Moreover, in order to improve the heat resistance of a bottle trunk | drum, the method of heat-processing by making the temperature of an extending | stretching blow metal mold high is taken, for example (for example, refer patent document 3). However, if a large number of bottles are continuously formed using the same mold by such a method, the bottle obtained with a long time operation is whitened, the transparency is lowered, and only a bottle having no commercial value can be obtained. . It has been found that this is due to adhesion of PET due to the PET surface on the mold surface, resulting in mold contamination, which is transferred to the bottle surface. In particular, in recent years, the molding speed has been increased along with the downsizing of the bottle. From the viewpoint of productivity, the melting time at the time of injection molding is shortened, the heating time for crystallization of the plug portion is shortened, or the mold. Contamination has become a greater problem and is not satisfactory with conventional PET, and a solution is desired.

  The polyester also contains acetaldehyde (hereinafter sometimes abbreviated as AA) as a by-product. When the content of acetaldehyde in the polyester is high, the content of acetaldehyde in the material such as a container molded from now on or other packaging also increases, which affects the flavor and odor of the beverage filled in the container. In recent years, polyester containers such as polyethylene terephthalate have come to be used as containers for low flavor beverages such as mineral water and oolong tea. In the case of such beverages, these beverages are generally heat-filled or sterilized by heating after filling, but it is becoming increasingly important to reduce the acetaldehyde content of the beverage container. In addition, for beverage metal cans, for the purposes of process simplification, hygiene, pollution prevention, etc., cans are made using a metal plate whose inner surface is coated with a polyester film whose main repeating unit is ethylene terephthalate. The method to do has come to be adopted. In this case as well, it is sterilized by heating at a high temperature after filling the contents. At this time, it is found that the use of a film having a sufficiently low acetaldehyde content is an essential requirement for improving the flavor and odor of the contents. I came.

  For these reasons, various measures have been taken to reduce the acetaldehyde content in the polyester. As these measures, for example, a method for reducing oligomers and aldehydes by subjecting a polyester prepolymer obtained by melt polymerization to solid phase polymerization under reduced pressure or under the flow of an inert gas (for example, Patent Document 4, 5), a method for crystallization and solid-phase polymerization after conditioning the polyester prepolymer so that the moisture content is 2000 ppm or more (see, for example, Patent Document 6), and heating the polyester particles with hot water at 50 to 200 ° C. After the treatment, a method of heat treatment under reduced pressure or inert gas flow (for example, see Patent Document 7), a method of extraction and washing with water or an organic solvent before and after solid phase polymerization (for example, see Patent Document 8) ) Etc. have been proposed. However, even with a molded body using polyester obtained by these methods, it cannot be said that oligomers and acetaldehyde can be reduced to a satisfactory level, and the problem has not been solved.

  As a method for further solving such problems, a method of deactivating the catalyst by contacting polyethylene terephthalate with water (see, for example, Patent Documents 9, 10, 11, and 12) and a catalyst by treating with water. Deactivated PET (see, for example, Patent Documents 13 and 14) is disclosed. However, such a catalyst deactivation method by contact treatment with water is effective only for polyesters produced using a germanium compound as a polycondensation catalyst, and produced using an antimony compound, a titanium compound, an aluminum compound or the like as a catalyst. Since there is little effect on the deactivation of these catalysts in the polyester, the increase in the AA content during molding cannot be suppressed, and the properties such as the flavor and odor of the contents of the molded product are hardly improved. In addition, since an apparatus and a drying apparatus for the processing are necessary, there is a problem that the capital investment cost and the processing cost are excessive, leading to an increase in cost and poor profitability.

  Further, a method is disclosed in which a polycondensation catalyst is deactivated by kneading a thermoplastic resin containing a phosphorus compound with PET (for example, see Patent Document 15). However, when a phosphorus compound-containing thermoplastic resin is produced using a general-purpose SUS304 polymerization can, there is a problem that the metal atom of the polymerization can elutes into the phosphorus compound-containing thermoplastic resin. It has been found that it becomes a crystal nucleus material for PET and not only lowers the transparency of a molded product obtained by mixing and using this resin in PET, but also affects the flavor. Thus, there exists a problem that it is difficult to always obtain a molded article excellent in transparency and flavor retention, and a solution is desired.

JP 55-79237 A JP 58-110221 A Japanese Examined Patent Publication No.59-6216 JP 55-89330 A JP 55-89331 A JP 59-219328 A JP 56-55426 A Japanese Patent Laid-Open No. 55-13715 Japanese Patent Laid-Open No. 3-47830 Japanese Patent Laid-Open No. 3-174441 Japanese Patent Laid-Open No. 6-234834 JP-A-8-231689 Japanese Patent Laid-Open No. 3-72524 JP-A-4-21424 Japanese Patent Laid-Open No. 10-251393

  The present invention deactivates the action of the polycondensation catalyst used at the time of producing the polyester, thereby producing the aldehydes such as acetaldehyde and cyclic oligomers at the time of molding and the deterioration of the transparency of the molded body. It can be used to solve problems such as, and the content of metal atoms eluted from the polymerization kettle has been reduced. The phosphorus-containing polyester resin has excellent transparency and flavor retention, and is a mold for continuous molding. An object of the present invention is to provide a polyester resin composition capable of efficiently producing a hollow molded article having no problem such as deterioration of transparency due to dirt and excellent in heat-resistant dimensional stability, and a molded article comprising the same. .

  In order to achieve the above object, the polyester resin of the present invention is a polyester resin mainly comprising an aromatic dicarboxylic acid component and a glycol component, and containing a phosphorus compound as a phosphorus atom in an amount of 100 to 10,000 ppm, and containing a Cr atom. It is a polyester resin characterized in that (Cr) and Fe atom content (Fe) satisfy the following formulas A and B.

Cr ≦ 10ppm (A)
Fe ≦ 30ppm (B)

  The polyester resin of the present invention is a polyester resin (1) containing a phosphorus compound as a phosphorus atom, preferably 200 to 8000 ppm, more preferably 300 to 6000 ppm, and the phosphorus atom in the polyester resin (1) is less than 100 ppm. The compatibility with the polyester resin (2) tends to decrease, and the haze of the molded product increases. On the other hand, if it exceeds 10,000 ppm, the polymerization rate becomes too fast and commercial production becomes difficult.

  Further, the Cr atom content and the Fe atom content in the polyester resin (1) are preferably 8 ppm or less and 25 ppm or less, respectively, more preferably 6 ppm or less and 20 ppm or less, respectively, as Cr atoms and Fe atoms. More preferably, they are 4 ppm or less and 10 ppm or less, respectively, Most preferably, they are 1 ppm or less and 5 ppm or less, respectively. Moreover, as Cr atom and Fe atom, all contain at least 0.05 ppm or more, usually 0.1 ppm or more. If the Cr atom content and the Fe atom content exceed 10 ppm and 30 ppm, respectively, the transparency of the molded product obtained from the polyester resin composition with the polyester resin (2) deteriorates, and the molded product is colored. It becomes intense and a problem.

  In this case, the polycondensation catalyst is preferably at least one selected from the group consisting of Sb compounds and Ge compounds.

  In this case, the polyester resin (1) is at least one selected from the group consisting of Al, Ti, Mn, Fe, Co, Zn, Nb, Mo, Cd, In, Sn, Ta, and Pb as a polycondensation catalyst. The catalyst of the polyester resin (2) can be deactivated by mixing with a polyester resin (2) mainly comprising an aromatic dicarboxylic acid component and a glycol component, which contains a compound containing any of the above elements and melt-treating it. It can be used as a polyester resin that has lost catalyst.

  In this case, the content of aldehydes in the polyester resin (1) is preferably 200 ppm or less.

  In this case, the phosphorus compound is at least one selected from the group consisting of a phosphoric acid compound, a phosphonic acid compound, a phosphinic acid compound, a phosphorous acid compound, a phosphonous acid compound, and a phosphinic acid compound. Preferably there is.

  In this case, the polyester resin (1) and a compound containing at least one element selected from the group consisting of Al, Ti, Mn, Fe, Co, Zn, Nb, Mo, Cd, In, Sn, Ta, and Pb A polyester resin composition comprising a polyester resin (2) mainly comprising an aromatic dicarboxylic acid component and a glycol component, which contains an antimony compound and / or a germanium compound as required.

  Further, the polyester resin composition has excellent flavor retention, low cyclic ester oligomer content, almost no occurrence of mold contamination during continuous molding, and thus excellent transparency and little variation in transparency. A molded body, for example, a hollow molded body, a sheet-like material, a stretched film, or the like, or a coating formed by melt-extruding the polyester composition on a substrate can be provided.

  The polyester resin of the present invention is a polyester resin that can be used to deactivate the polycondensation catalyst used in the production of polyester and suppress the formation of aldehydes such as acetaldehyde and cyclic oligomers during molding. The polyester resin composition comprising the same has a very low metal elution amount at the time of melt polymerization, excellent flavor retention, and almost no occurrence of mold fouling at the time of continuous molding. Therefore, there is little variation in transparency and transparency. A molded body, particularly a hollow molded body or a coating on a base material is provided. Also, operability is improved.

  Hereinafter, embodiments of the polyester resin and the polyester resin composition of the present invention and their uses will be specifically described.

(Polyester resin (1))
Examples of the phosphorus compound copolymerized or blended with the polyester resin (1) of the present invention include phosphoric acid compounds, phosphonic acid compounds, phosphinic acid compounds, phosphorous acid compounds, phosphonous acid compounds, and phosphinic acid. System compounds.

Specific examples of phosphoric acid compounds include, for example, phosphoric acid, dimethyl phosphate, diethyl phosphate, dipropyl phosphate, dibutyl phosphate, diamyl phosphate, dihexyl phosphate, trimethyl phosphate, triethyl phosphate, tripropyl phosphate, tributyl phosphate, triamyl Examples thereof include phosphate, trihexyl phosphate, ester of phosphoric acid and alkylene glycol, and the like.
Specific examples of phosphonic acid compounds include, for example, methylphosphonic acid, dimethyl methylphosphonate, diphenyl methylphosphonate, phenylphosphonic acid, dimethyl phenylphosphonate, diphenyl phenylphosphonate, dimethyl phosphophosphonate, diethyl benzylphosphonate, triethylphosphono Examples include acetate, tributylphosphonoacetate, tri (hydroxyethyl) phosphonoacetate, tri (hydroxypropyl) phosphonoacetate, tri (hydroxybutyl) phosphonoacetate and the like.

  Specific examples of the phosphinic acid compounds include, for example, diphenylphosphinic acid, methyl diphenylphosphinate, phenyl diphenylphosphinate, phenylphosphinic acid, methyl phenylphosphinate, phenyl phenylphosphinate, 2-carboxyethyl-methylphosphinic acid, 2 -Carboxyethyl-ethylphosphinic acid, 2-carboxyethyl-propylphosphinic acid, 2-carboxyethyl-phenylphosphinic acid, 2-carboxyethyl-m-toluylphosphinic acid, 2-carboxyethyl-p-toluylphosphinic acid, 2- Carboxyethyl-xylylphosphinic acid, 2-carboxyethyl-benzylphosphinic acid, 2-carboxyethyl-m-ethylbenzylphosphinic acid, 2-carboxymethyl-methylphosphinic acid, 2 Carboxymethyl-ethylphosphinic acid, 2-carboxyethyl-propylphosphinic acid, 2-carboxymethyl-phenylphosphinic acid, 2-carboxymethyl-m-toluylphosphinic acid, 2-carboxymethyl-p-toluylphosphinic acid, 2-carboxy Methyl-xylylphosphinic acid, 2-carboxymethyl-benzylphosphinic acid, 2-carboxymethyl-m-ethylbenzylphosphinic acid, and cyclic anhydrides thereof, or methyl ester, ethyl ester, propyl ester, butyl ester thereof , Ethylene glycol ester, propion glycol ester, ester with butanediol, and the like.

Specific examples of phosphorous compounds include, for example, phosphorous acid and dimethyl phosphite, diethyl phosphite, dipropyl phosphite, dibutyl phosphite, diamyl phosphite, dihexyl phosphite, trimethyl phosphite, triethyl phosphite , Triphenyl phosphite, tris (2,4-di-tert-butylphenyl) phosphite, tetrakis (2,4-di-tert-butylphenyl) 4,4′-biphenylene diphosphite, phosphorous acid and alkylene Examples include esters with glycols.
Specific examples of the phosphonous compound include methylphosphonous acid, dimethyl methylphosphonite, diphenyl methylphosphonite, phenylphosphonite, dimethyl phenylphosphonite, and phenyl phenylphosphonite. .

  As other phosphorus compounds, phosphorus compounds other than those used in the following polyester resin (2) can also be used.

  The polyester resin (1) according to the present invention is a thermoplastic polyester mainly obtained from an aromatic dicarboxylic acid component and a glycol component, and preferably a polyester in which an aromatic dicarboxylic acid unit contains 70 mol% or more of the acid component. More preferably, it is a polyester containing 80 mol% or more of the aromatic dicarboxylic acid unit of the acid component, more preferably a polyester containing 85 mol% or more of the aromatic dicarboxylic acid unit of the acid component, and particularly preferably aromatic polyester. A polyester in which a group dicarboxylic acid unit contains 90 mol% or more of the acid component, and is a copolymer or blend of the above phosphorus compound.

Examples of the aromatic dicarboxylic acid component constituting the polyester resin (1) according to the present invention include aromatics such as terephthalic acid, 2,6-naphthalenedicarboxylic acid, diphenyl-4,4′-dicarboxylic acid, and diphenoxyethanedicarboxylic acid. Examples thereof include dicarboxylic acids and functional derivatives thereof.
Examples of the glycol component constituting the polyester resin (1) according to the present invention include aliphatic glycols such as ethylene glycol, 1,3-trimethylene glycol and tetramethylene glycol, and alicyclic glycols such as cyclohexanedimethanol. It is done.

  Examples of the dicarboxylic acid used as a copolymerization component when the polyester is a copolymer include isophthalic acid, diphenyl-4,4′-dicarboxylic acid, diphenoxyethanedicarboxylic acid, and 4,4′-diphenyl ether dicarboxylic acid. , Aromatic dicarboxylic acids such as 4,4′-diphenyl ketone dicarboxylic acid and functional derivatives thereof, oxyacids such as p-oxybenzoic acid and oxycaproic acid and functional derivatives thereof, adipic acid, sebacic acid, succinic acid, Examples thereof include aliphatic dicarboxylic acids such as glutaric acid and dimer acid and functional derivatives thereof, and alicyclic dicarboxylic acids such as hexahydroterephthalic acid, hexahydroisophthalic acid and cyclohexanedicarboxylic acid, and functional derivatives thereof.

  The glycol as a copolymerization component used when the polyester is a copolymer is diethylene glycol, 1,3-trimethylene glycol, tetramethylene glycol, pentamethylene glycol, hexamethylene glycol, octamethylene glycol, decamethylene. Glycols, 2-ethyl-2-butyl-1,3-propanediol, aliphatic glycols such as neopentyl glycol, dimer glycol, 1,2-cyclohexanediol, 1,4-cyclohexanediol, 1,1-cyclohexanedimethylol 1,4-cyclohexane dimethylol, 2,5-norbornane dimethylol and other alicyclic glycols, xylylene glycol, 4,4′-dihydroxybiphenyl, 2,2-bis (4′-β-hydroxyethoxy) Aromatic glycols such as phenyl) propane, bis (4-hydroxyphenyl) sulfone, bis (4-β-hydroxyethoxyphenyl) sulfonic acid, and alkylene oxide adducts of bisphenol A, polyalkylene glycols such as polyethylene glycol and polybutylene glycol Etc.

  Furthermore, examples of the polyfunctional compound as a copolymer component used when the polyester is a copolymer include trimellitic acid, pyromellitic acid, and the like as an acid component, and glycerin and pentane as glycol components. Mention may be made of erythritol. The amount of copolymerization component used should be such that the polyester remains substantially linear. Monofunctional compounds such as benzoic acid and naphthoic acid may be copolymerized.

  A preferred example of the polyester resin (1) according to the present invention is a polyester whose main structural unit is composed of ethylene terephthalate, more preferably 70 mol% or more of ethylene terephthalate units, and isophthalic acid, 2, It is a copolyester containing 6-naphthalenedicarboxylic acid, 1,4-cyclohexanedimethanol, etc., particularly preferably a polyester containing 90 mol% or more of ethylene terephthalate units, wherein the above phosphorus compound is copolymerized or blended. Is.

  The polyester resin (1) copolymerized or blended with the phosphorus compound of the present invention is a method of copolymerizing by adding the phosphorus compound at the time of polycondensation, or at least one selected from the polyester resin and the phosphorus compound as an extruder, for example, Although it can be produced by a method of kneading with a twin screw extruder, it is not limited thereto.

  In the case of a copolymerization method, for example, in the case of a copolymer polyester from terephthalic acid, ethylene glycol and a phosphorus compound, a polyester obtained by polycondensation of the reaction product of terephthalic acid and / or an ester-forming derivative thereof and ethylene glycol is used. It can be produced by an arbitrary method employed in the process.

  As a reactor for performing esterification reaction or polycondensation reaction, high temperature corrosion resistance more than SUS316, SUS316L, SUS317, SUS317L, Hastelloy is required, preferably SUS316L, SUS317, SUS317L, Hastelloy, most preferably SUS317, SUS317L It is preferable to use a Hastelloy reactor, a stirrer, etc., but is not limited thereto. In particular, as a reactor in which an unreacted phosphorus compound is present at a high concentration or a reactor in which a phosphorus compound is reacted at 230 ° C. or higher, it is preferable to use the high corrosion resistance reactor. In a reactor made of a metal material generally used for polycondensation of PET, a large amount of Cr metal or Fe metal is not preferable.

  The phosphorus compound is added during the production of the polyester, and the addition time can be added at any stage from the early stage of the esterification process to the late stage of the initial condensation. It is preferable to add from the latter stage of the esterification step to the early stage of the initial condensation because of corrosion problems.

  Preferred manufacturing conditions are as follows. That is, the esterification reaction is carried out at 230 to 250 ° C. under normal pressure to increased pressure for 0.5 to 5 hours so that the esterification reaction rate is at least 90%, preferably 95% or more. Next, a phosphorus compound is added, and the first stage polycondensation is performed at 240 to 255 ° C., preferably 240 to 250 ° C., more preferably 240 to 248 ° C. at 300 to 0.1 Torr for 0.5 to 2 hours, Further, the polycondensation is carried out at 250 to 280 ° C., preferably 250 to 278 ° C., more preferably 250 to 275 ° C. at 10 to 0.1 Torr, preferably 5 to 0.1 Torr to the desired degree of polymerization. In particular, it is important to carry out the first stage polycondensation reaction at 250 ° C. or lower in order to achieve the object of the present invention.

  Examples of the starting material terephthalic acid or ethylene glycol include virgin terephthalic acid derived from para-xylene or ethylene glycol derived from ethylene, as well as methanol decomposition and ethylene glycol decomposition from used PET bottles. A recovered raw material such as terephthalic acid, bishydroxyethyl terephthalate or ethylene glycol recovered by the chemical recycling method can also be used as at least a part of the starting raw material. Needless to say, the quality of the recovered raw material must be refined to a purity and quality suitable for the intended use.

  Polycondensation catalysts include lithium, sodium, potassium, rubidium, cesium, beryllium, magnesium, calcium, strontium, indium, thallium, germanium, tin, lead, bismuth, scandium, yttrium, niobium, zirconium, hafnium, vanadium, chromium, One or more metal compounds selected from the group consisting of manganese, iron, cobalt, nickel, copper, zinc, ruthenium, rhodium, palladium, tellurium, tantalum, tungsten, gallium, aluminum, antimony, germanium, titanium, silicon, silver, etc. In particular, antimony compounds, germanium compounds, and tungsten compounds, which are not deactivated by the phosphorus compounds, are most suitable.

  Specific examples of the Sb compound include antimony trioxide, antimony acetate, antimony tartrate, antimony tartrate, antimony oxychloride, antimony glycolate, antimony pentoxide, and triphenylantimony. The Sb compound is added so that the residual amount of Sb in the produced polymer is in the range of 50 to 300 ppm, preferably 55 to 250 ppm, more preferably 60 to 200 ppm.

  Specific examples of the Ge compound include amorphous germanium dioxide, crystalline germanium dioxide, germanium tetroxide, germanium hydroxide, germanium oxalate, germanium chloride, germanium tetraethoxide, germanium tetra-n-butoxide, and germanium phosphite. And the like. When a Ge compound is used, the amount used is 10 to 100 ppm, preferably 11 to 80 ppm, more preferably 13 to 50 ppm as the residual amount of Ge in the polyester resin (1).

  In the production of the polyester resin (1) of the present invention, a basic nitrogen compound can be used in order to suppress the dialkylene glycol content within the following range. As the basic nitrogen compound, any of aliphatic, alicyclic, aromatic and heterocyclic nitrogen compounds may be used. Specific examples include triethylamine, tributylamine, dimethylaniline, dimethylaniline, pyridine, quinoline, dimethylbenzylamine, piperidine, tetraethylammonium hydroxide, tetrabutylammonium hydroxide, triethylbenzylammonium hydroxide, imidazole, imidazoline, and the like. . These compounds may be used in free form or as a salt of lower fatty acid or TPA. The addition of these basic nitrogen compounds to the reaction system can be appropriately selected at any stage until the initial polycondensation reaction is completed, and may be used alone or in combination of two or more. Good. The compounding amount of these basic nitrogen compounds is 0.01 to 1 mol%, preferably 0.05 to 0.7 mol%, more preferably 0.1 to 0.5 mol% per polyester.

  The polyester resin polycondensed as described above is transported from the final melt polycondensation reactor to the nozzle in a molten state, for example, a method in which molten polyester is extruded into water through die pores and cut in water, or a die After being extruded in the form of strands from the pores into the air, the chips are formed into columns, spheres, squares or plates by a method of forming chips while cooling with cooling water. At this time, it is necessary to obtain the polyester resin (1) of the present invention by making the temperature in the molten state up to the nozzle as low as possible and making the residence time as short as possible. is there.

  Moreover, as the cooling water at the time of chip formation of the melt polycondensed polyester, it is preferable to use cooling water satisfying at least one of the following (1) to (4), and more preferably (1) to (4 It is most preferable to use water that satisfies all of the above.

Na ≦ 1.0 (ppm) (1)
Mg ≦ 1.0 (ppm) (2)
Si ≦ 2.0 (ppm) (3)
Ca ≦ 1.0 (ppm) (4)

  The sodium content (Na) in the cooling water is preferably Na ≦ 0.5 ppm, more preferably Na ≦ 0.1 ppm. The magnesium content (Mg) in the cooling water is preferably Mg ≦ 0.5 ppm, more preferably Mg ≦ 0.1 ppm. Further, the content (Si) of silicon in the cooling water is preferably Si ≦ 0.5 ppm, more preferably Si ≦ 0.3 ppm. Furthermore, the calcium content (Ca) in the cooling water is preferably Ca ≦ 0.5 ppm, and more preferably Ca ≦ 0.1 ppm.

  In order to reduce sodium, magnesium, calcium, and silicon in the cooling water, an apparatus for removing sodium, magnesium, calcium, and silicon is installed in at least one place until the industrial water is sent to the chip cooling process. Also, a filter is installed to remove clay minerals such as silicon dioxide and aluminosilicate particles. Examples of the device for removing sodium, magnesium, calcium, and silicon include an ion exchange device, an ultrafiltration device, and a reverse osmosis membrane device.

  Although the polyester resin (1) of this invention is manufactured as mentioned above, in addition to these, the method shown below can be employ | adopted suitably. That is, a method in which a melt polycondensation polymer having an IV of 0.55 deciliter / gram or more is crystallized by heating at a temperature of up to 150 ° C. under reduced pressure or under an inert gas flow immediately after chipping, and an IV of 0.40 to 0.4. A technique of solid phase polymerization of 60 deciliter / gram solution polycondensation prepolymer can be used. Moreover, the method of melt-extruding polyester with a vent type extruder under pressure reduction or an inert gas distribution can be used. Moreover, the method of heat-processing a phosphorus containing polyester resin with organic solvents, such as water and chloroform, can also be used. Moreover, these methods can also be combined appropriately.

  In addition, in the case of using a method of blending a phosphorus compound with a polyester resin, a method of melt-kneading the dried polyester resin and the phosphorus compound with a twin screw extruder into a chip, an aqueous solution of a phosphorus compound or an organic solvent This is possible by a method of immersing in the above solution or a method of attaching these solutions to the surface.

Also in this case, it is preferable to use a twin screw extruder composed of SUS316 or more, preferably SUS316L, SUS317, SUS317L, a Hastelloy screw or barrel.
The intrinsic viscosity of the polyester resin (1) of the present invention is 0.50 to 1.00 deciliter / gram, preferably 0.57 to 0.90 deciliter / gram, more preferably 0.60 to 0.85 deciliter / gram. The most preferable range is 0.69 to 0.80 deciliter / gram.

  When the intrinsic viscosity is 0.60 deciliter / gram or more, it is preferable to use a method in which a polymer obtained by melt polycondensation is polymerized in a solid state.

  When the intrinsic viscosity is less than 0.50 deciliter / gram, the transparency of the obtained molded article is deteriorated, and the mechanical strength does not satisfy the practical range. On the other hand, when it exceeds 1.00 deciliter / gram, kneading is incomplete when a composition with the polyester resin (2) is molded, and a molded product of uniform quality cannot be obtained.

  The content of dialkylene glycol copolymerized with the polyester resin (1) of the present invention is preferably 1.0 to 10 mol%, more preferably 2.0 to 8% of the glycol component constituting the polyester. It is desirable that the amount be 0.0 mol%, more preferably 2.0 to 6.0 mol%. When the amount of dialkylene glycol exceeds 10 mol%, the thermal stability is deteriorated, the molecular weight is greatly reduced during molding, and the increase in the content of aldehydes is increased, which is not preferable. Here, the dialkylene glycol copolymerized in the polyester, for example, in the case of a polyester whose main structural unit is ethylene terephthalate, is a diethylene glycol by-produced during production from ethylene glycol, which is a glycol. Among them, diethylene glycol (hereinafter abbreviated as DEG) copolymerized with the polyester, and in the case of a polyester having 1,3-propylene terephthalate as a main constituent unit, is glycol 1 Among di (1,3-propylene glycol) (or bis (3-hydroxypropyl) ether) produced as a by-product during production from 1,3-propylene glycol, di (1,3) copolymerized with the polyester -Propylene glycol).

  The content of the aldehydes contained in the polyester resin (1) of the present invention is 200 ppm or less, preferably 150 ppm or less, more preferably 100 ppm or less, and most preferably 50 ppm or less. When the content of aldehydes exceeds 200 ppm, the flavor retention of the contents of the molded product obtained from the polyester composition of the present invention becomes very poor, causing problems. Further, the lower limit of the content of aldehydes is 1 ppm, preferably 2 ppm, more preferably 3 ppm from the viewpoint of economical production. Here, the aldehydes are those in which the polyester resin (1) is ethylene glycol such as polyester having ethylene terephthalate as a main structural unit or polyester having ethylene-2,6-naphthalate as a main structural unit. In the case of polyester as the main component of the glycol component, it is acetaldehyde or formaldehyde, in the case of polyester having 1,3-propylene terephthalate as the main structural unit, it is allylaldehyde, and further, butylene terephthalate is the main structural unit. In the case of polyester, it is butanal. However, in the case of a polyester having butylene terephthalate as the main structural unit, the aldehyde is mostly detected as tetrahydrofuran.

In addition, as a method of setting the content of aldehydes in the polyester resin (1) of the present invention to 200 ppm or less, a method of solid-phase polymerization of a solution-polymerized polyester prepolymer having an IV of 0.30 to 0.60, a predetermined IV A method of heat-treating polyester under an inert gas atmosphere or under reduced pressure under conditions where IV does not substantially change, a method of heat-treating polyester at a temperature of 50 to 180 ° C. in an inert air current, or a polyester vent type Methods such as melt extrusion under reduced pressure or inert gas flow in an extruder can be used alone or in appropriate combination.
When the polyester resin (1) of the present invention is used for catalyst deactivation of the polyester resin (2) for a high heat-resistant hollow molded article, the cyclic trimer content of the polyester resin (1) is 8000 ppm or less. , Preferably 7500 ppm or less, more preferably 7000 ppm or less. When the cyclic trimer content exceeds 8000 ppm, the mold becomes very dirty, and a hollow molded article having excellent transparency cannot be obtained during long-time molding. The lower limit of the cyclic trimer content is 3000 ppm, preferably 3500 ppm, more preferably 4000 ppm from the viewpoint of economical production. In addition, as a method of reducing cyclic trimer content to 8000 ppm or less, the method of reducing the aldehyde described above can be used.

The shape of the chip of the polyester resin (1) of the present invention may be any of a cylinder shape, a square shape, a spherical shape or a flat plate shape. The average particle diameter is usually 1.0 to 4 mm, preferably 1.0 to 3.5 mm, and more preferably 1.0 to 3.0 mm. For example, in the case of a cylinder type, it is practical that the length is about 1.0 to 4 mm and the diameter is about 1.0 to 4 mm. In the case of spherical particles, it is practical that the maximum particle size is 1.1 to 2.0 times the average particle size and the minimum particle size is 0.7 times or more the average particle size. The weight of the chip is practically in the range of 2 to 40 mg / piece.
In addition, in the process of forming the polyester resin (1), the step of forming the melt polycondensation polymer into chips, the solid phase polymerization step, the step of transporting the melt polycondensation polymer chip or the solid phase polymerization polymer chip, etc. Particles and powders that are considerably smaller than the chips of a set size are sometimes generated. Here, such a fine granular material or powder is referred to as fine.

Such fines have the property of promoting crystallization of the molded product from the polyester resin composition, and it is important to control the fine content of the polyester resin (1) to 1% by weight or less. When the fine content exceeds 1% by weight, the transparency of the molded article molded from the composition with the polyester resin (2) is deteriorated, the crystallization speed is high, and the fluctuation is very fast. These problems occur, and a polyester resin composition and a polyester molded body that achieve the object of the present invention cannot be obtained. The lower limit of the fine content of the polyester resin (1) is about 10 ppm or less, and making it lower is a problem in terms of economy.
As a method of making content of the fine in a polyester resin (1) 1 weight% or less, the method of passing through the fine removal process by a sieving process or an airflow, etc. are employable, for example.

  Also, conventionally known UV absorbers, antioxidants, oxygen scavengers, lubricants added from the outside, lubricants that have been precipitated internally during the reaction, mold release agents, cores to the extent that physical properties such as polymer color and hydrolyzability are not impaired. Various additives such as an agent, a stabilizer, an antistatic agent, a bluing agent, a dye, and a pigment can be used in combination.

(Polyester resin (2))
The polyester resin (2) is a thermoplastic polyester mainly obtained from an aromatic dicarboxylic acid component and a glycol component, preferably a polyester containing 70 mol% or more of the aromatic dicarboxylic acid unit of the acid component, more preferably aromatic polyester. A polyester containing 80 mol% or more of an aromatic dicarboxylic acid unit, more preferably a polyester containing 85 mol% or more of an aromatic dicarboxylic acid unit, and particularly preferably an aromatic dicarboxylic acid unit containing an acid component. Polyester containing 90 mol% or more.

  Examples of the aromatic dicarboxylic acid component constituting the polyester resin (2) according to the present invention include aromatics such as terephthalic acid, 2,6-naphthalenedicarboxylic acid, diphenyl-4,4′-dicarboxylic acid, and diphenoxyethanedicarboxylic acid. Examples thereof include dicarboxylic acids and functional derivatives thereof.

  Examples of the glycol component constituting the polyester resin (2) according to the present invention include aliphatic glycols such as ethylene glycol, 1,3-trimethylene glycol, and tetramethylene glycol, and alicyclic glycols such as cyclohexanedimethanol. Can be mentioned.

  Examples of the dicarboxylic acid used as a copolymerization component when the polyester is a copolymer include isophthalic acid, diphenyl-4,4′-dicarboxylic acid, diphenoxyethanedicarboxylic acid, and 4,4′-diphenyl ether dicarboxylic acid. , Aromatic dicarboxylic acids such as 4,4′-diphenyl ketone dicarboxylic acid and functional derivatives thereof, oxyacids such as p-oxybenzoic acid and oxycaproic acid and functional derivatives thereof, adipic acid, sebacic acid, succinic acid, Examples thereof include aliphatic dicarboxylic acids such as glutaric acid and dimer acid and functional derivatives thereof, and alicyclic dicarboxylic acids such as hexahydroterephthalic acid, hexahydroisophthalic acid and cyclohexanedicarboxylic acid, and functional derivatives thereof.

  The glycol as a copolymerization component used when the polyester is a copolymer is diethylene glycol, 1,3-trimethylene glycol, tetramethylene glycol, pentamethylene glycol, hexamethylene glycol, octamethylene glycol, decamethylene. Glycols, 2-ethyl-2-butyl-1,3-propanediol, aliphatic glycols such as neopentyl glycol, dimer glycol, 1,2-cyclohexanediol, 1,4-cyclohexanediol, 1,1-cyclohexanedimethylol 1,4-cyclohexane dimethylol, 2,5-norbornane dimethylol and other alicyclic glycols, xylylene glycol, 4,4′-dihydroxybiphenyl, 2,2-bis (4′-β-hydroxyethoxy) Aromatic glycols such as phenyl) propane, bis (4-hydroxyphenyl) sulfone, bis (4-β-hydroxyethoxyphenyl) sulfonic acid, and alkylene oxide adducts of bisphenol A, polyalkylene glycols such as polyethylene glycol and polybutylene glycol Etc.

  Furthermore, examples of the polyfunctional compound as a copolymer component used when the polyester is a copolymer include trimellitic acid, pyromellitic acid, and the like as an acid component, and glycerin and pentane as glycol components. Mention may be made of erythritol. The amount of copolymerization component used should be such that the polyester remains substantially linear. Monofunctional compounds such as benzoic acid and naphthoic acid may be copolymerized.

  A preferred example of the polyester resin (2) according to the present invention is a polyester whose main structural unit is composed of ethylene terephthalate, preferably 55 mol% or more, more preferably 70 mol% or more of ethylene terephthalate units, and copolymerization. It is a copolyester containing isophthalic acid, 2,6-naphthalenedicarboxylic acid, 1,4-cyclohexanedimethanol and the like as a component, particularly preferably a polyester containing 90 mol% or more of ethylene terephthalate units.

  Examples of these polyesters include polyethylene terephthalate (hereinafter abbreviated as PET), poly (ethylene terephthalate-ethylene isophthalate) copolymer, poly (ethylene terephthalate-ethylene-2,6-naphthalate) copolymer, poly (ethylene). Terephthalate-1,4-cyclohexanedimethylene terephthalate) copolymer, poly (ethylene terephthalate-dioxyethylene terephthalate) copolymer, poly (ethylene terephthalate-1,3-propylene terephthalate) copolymer, poly (ethylene terephthalate-) Ethylene cyclohexylene dicarboxylate) copolymer and the like.

Further, another preferred example of the polyester resin (2) according to the present invention is a polyester in which the main structural unit is composed of ethylene-2,6-naphthalate, and preferably 55 moles of ethylene-2,6-naphthalate units. % Or more, more preferably 70 mol% or more of the polyester, particularly preferably polyester containing 90 mol% or more of ethylene-2,6-naphthalate units.
Examples of these thermoplastic polyesters include polyethylene-2,6-naphthalate (PEN), poly (ethylene-2,6-naphthalate-ethylene terephthalate) copolymer, poly (ethylene-2,6-naphthalate-ethylene isophthalate). ) Copolymer, poly (ethylene-2,6-naphthalate-dioxyethylene-2,6-naphthalate) copolymer, and the like.

In addition, another preferable example of the polyester resin (2) according to the present invention is a polyester in which the main structural unit is composed of 1,3-propylene terephthalate, and preferably 55 mol% of 1,3-propylene terephthalate units. Above, more preferably a polyester containing 70 mol% or more, particularly preferably a polyester containing 90 mol% or more of 1,3-propylene terephthalate units.
Examples of these polyesters include polypropylene terephthalate (PTT), poly (1,3-propylene terephthalate-1,3-propylene isophthalate) copolymer, poly (1,3-propylene terephthalate-1,4-cyclohexanedimethylene). Terephthalate) copolymer and the like.

  Furthermore, other preferable examples of the polyester resin (2) according to the present invention are polyesters in which the main structural unit is composed of butylene terephthalate, preferably 55 mol% or more, more preferably 70 mol of butylene terephthalate units. %, Particularly preferably a polyester containing 90 mol% or more of butylene terephthalate units.

  Examples of these polyesters include polybutylene terephthalate (PBT), poly (butylene terephthalate-butylene isophthalate) copolymer, poly (butylene terephthalate-1,4-cyclohexanedimethylene terephthalate) copolymer, poly (butylene terephthalate- 1,3-propylene terephthalate) copolymer, poly (butylene terephthalate-butylene cyclohexylene dicarboxylate) copolymer, and the like.

  The polyester resin (2) according to the present invention can basically be produced by a conventionally known melt polycondensation method or a solid state polymerization method of a prepolymer produced by this method. The melt polycondensation reaction may be performed in one stage or may be performed in multiple stages. These may be comprised from a batch-type reaction apparatus, and may be comprised from the continuous-type reaction apparatus. The melt polycondensation step and the solid phase polymerization step may be operated continuously or may be operated separately.

  Hereinafter, an example of a preferable continuous production method of the polyester resin (2) according to the present invention will be described using polyethylene terephthalate (PET) as an example, but the present invention is not limited thereto. That is, a direct esterification method in which terephthalic acid is directly reacted with ethylene glycol and, if necessary, other copolymerization components to distill off water and esterify, followed by polycondensation under reduced pressure in the presence of a polycondensation catalyst, or , Produced by a transesterification method in which dimethyl terephthalate, ethylene glycol, and other copolymerization components as required are reacted to distill off methyl alcohol and transesterify, followed by polycondensation under reduced pressure in the presence of a polycondensation catalyst. Is done. In addition, in order to increase the intrinsic viscosity, and to achieve a low acetaldehyde content and a low cyclic trimer content, such as a heat-resistant container for low flavor beverages and a film for the inner surface of a metal can for beverages, The resulting melt polycondensed polyester is subsequently subjected to solid state polymerization.

  Examples of the starting materials dimethyl terephthalate, terephthalic acid or ethylene glycol include virgin dimethyl terephthalate derived from paraxylene, ethylene glycol derived from terephthalic acid or ethylene, and methanol from used PET bottles. Recovered raw materials such as dimethyl terephthalate, terephthalic acid, bishydroxyethyl terephthalate or ethylene glycol recovered by chemical recycling methods such as decomposition and ethylene glycol decomposition can also be used as at least part of the starting material. Needless to say, the quality of the recovered raw material must be refined to a purity and quality suitable for the intended use.

  The polycondensation reaction is performed using a polycondensation catalyst. As the polycondensation catalyst, a compound containing at least one element selected from the group consisting mainly of Al, Ti, Mn, Fe, Co, Zn, Nb, Mo, Cd, In, Sn, Ta, and Pb, and as required It is preferable to use at least one selected from second metal compounds such as Ge compounds and Sb compounds. These compounds are added to the reaction system as powders, aqueous solutions, ethylene glycol solutions, ethylene glycol slurries and the like.

  Specific examples of the Ti compound include tetraalkyl titanates such as tetraethyl titanate, tetraisopropyl titanate, tetra-n-propyl titanate, tetra-n-butyl titanate, and partial hydrolysates thereof, titanium acetate, titanyl oxalate. , Titanyl ammonium oxalate, sodium titanyl oxalate, potassium titanyl oxalate, calcium titanyl oxalate, titanium strontium oxalate, titanyl oxalate, titanium trimellitic acid, titanium sulfate, titanium chloride, titanium halide hydrolysate, titanium oxalate From titanium fluoride, potassium hexafluorotitanate, ammonium hexafluorotitanate, cobalt hexafluorotitanate, manganese hexafluorotitanate, titanium acetylacetonate, titanium and silicon or zirconium Composite oxides, reaction products of titanium alkoxides and phosphorus compounds, reaction products obtained by reacting phosphorus compounds with reaction products of titanium alkoxides and aromatic polycarboxylic acids or their anhydrides, etc. It is done. The Ti compound is added so that the remaining amount of Ti in the produced polymer is in the range of 0.1 to 50 ppm.

  Specific examples of the Al compound include aluminum formate, aluminum acetate, basic aluminum acetate, aluminum propionate, aluminum oxalate, aluminum acrylate, aluminum laurate, aluminum stearate, aluminum benzoate, aluminum trichloroacetate, and aluminum lactate. , Carboxylates such as aluminum citrate and aluminum salicylate, inorganic acid salts such as aluminum chloride, aluminum hydroxide, aluminum hydroxide chloride, polyaluminum chloride, aluminum nitrate, aluminum sulfate, aluminum carbonate, aluminum phosphate and aluminum phosphonate Aluminum methoxide, Aluminum ethoxide, Aluminum n-propoxide, Aluminum iso-propoxide, Aluminum n-bub Aluminum alkoxides such as oxide and aluminum t-butoxide, aluminum chelate compounds such as aluminum acetylacetonate, aluminum acetylacetate, aluminum ethylacetoacetate, aluminum ethylacetoacetate diiso-propoxide, and organoaluminum compounds such as trimethylaluminum and triethylaluminum And a partial hydrolyzate thereof, aluminum oxide and the like. Of these, carboxylates, inorganic acid salts and chelate compounds are preferred, and among these, basic aluminum acetate, aluminum chloride, aluminum hydroxide, aluminum hydroxide chloride and aluminum acetylacetonate are particularly preferred. The Al compound is added so that the remaining amount of Al in the produced polymer is in the range of 5 to 200 ppm.

  Moreover, in the manufacturing method of the polyester resin (2) based on this invention, you may use together an alkali metal compound or an alkaline-earth metal compound. The alkali metal or alkaline earth metal is preferably at least one selected from Li, Na, K, Rb, Cs, Be, Mg, Ca, Sr, and Ba, and the use of an alkali metal or a compound thereof is preferable. More preferred. When using an alkali metal or a compound thereof, use of Li, Na, K is particularly preferable. Examples of the alkali metal and alkaline earth metal compounds include saturated aliphatic carboxylates such as formic acid, acetic acid, propionic acid, butyric acid, and succinic acid, and unsaturated aliphatic carboxylates such as acrylic acid and methacrylic acid. , Aromatic carboxylates such as benzoic acid, halogen-containing carboxylates such as trichloroacetic acid, hydroxycarboxylates such as lactic acid, citric acid and salicylic acid, carbonic acid, sulfuric acid, nitric acid, phosphoric acid, phosphonic acid, hydrogen carbonate, phosphorus Inorganic acid salts such as acid hydrogen, hydrogen sulfide, sulfurous acid, thiosulfuric acid, hydrochloric acid, hydrobromic acid, chloric acid and bromic acid, and organic sulfonates such as 1-propanesulfonic acid, 1-pentanesulfonic acid and naphthalenesulfonic acid , Organic sulfates such as lauryl sulfate, methoxy, ethoxy, n-propoxy, iso-propoxy, n-butoxy, tert-butyl Alkoxides such as alkoxy, chelate compounds and the like acetylacetonate, hydrides, oxides, and hydroxides and the like.

  The alkali metal compound or alkaline earth metal compound is added to the reaction system as a powder, an aqueous solution, an ethylene glycol solution, or the like. The alkali metal compound or alkaline earth metal compound is added so that the residual amount of these elements in the produced polymer is in the range of 1 to 100 ppm.

  The polycondensation catalyst used in the present invention is preferably used in combination with a phosphorus compound.

  The P compound used in the present invention is at least one selected from the group consisting of phosphonic acid compounds, phosphinic acid compounds, phosphine oxide compounds, phosphonous acid compounds, phosphinic acid compounds, and phosphine compounds. It is preferably a phosphorus compound. When an Al compound is used as the polycondensation catalyst, it is preferably used in combination with a phosphorus compound, and is preferably used as a solution or slurry in which an aluminum compound and a phosphorus compound are previously mixed in a solvent. By using these phosphorus compounds, an effect of improving the catalytic activity is seen, and an effect of improving physical properties such as thermal stability of the polyester is seen. Among these, use of a phosphonic acid compound is preferable because of its great effect of improving physical properties and improving catalytic activity. Among the above-described phosphorus compounds, the use of a compound having an aromatic ring structure is preferable because the physical property improving effect and the catalytic activity improving effect are great.

  The phosphonic acid-based compound, phosphinic acid-based compound, phosphine oxide-based compound, phosphonous acid-based compound, phosphinic acid-based compound, and phosphine-based compound referred to in the present invention are represented by the following formulas (1) to (6), respectively. A compound having a structure.

  Examples of the phosphonic acid compound used in the present invention include dimethyl methylphosphonate, diphenyl methylphosphonate, dimethyl phenylphosphonate, diethyl phenylphosphonate, diphenyl phenylphosphonate, dimethyl phosphophosphonate, diethyl benzylphosphonate, and the like. . Examples of the phosphinic acid compound used in the present invention include diphenylphosphinic acid, methyl diphenylphosphinate, phenyl diphenylphosphinate, phenylphosphinic acid, methyl phenylphosphinate, and phenylphenylphosphinate. Examples of the phosphine oxide compound used in the present invention include diphenylphosphine oxide, methyldiphenylphosphine oxide, and triphenylphosphine oxide.

Among the phosphinic acid compounds, phosphine oxide compounds, phosphonous acid compounds, phosphinic acid compounds, and phosphine compounds, compounds represented by the following formulas (7) to (12) are preferably used.

Among the phosphorus compounds described above, the use of a compound having an aromatic ring structure is preferable because the effect of improving the catalytic activity is great.

  Moreover, as a phosphorus compound used by this invention, when the compound represented by following General formula (13)-(15) is used, especially the improvement effect of a catalyst activity is large and preferable.

(In the formulas (13) to (15), R ¹ , R ⁴ , R ⁵ and R ⁶ each independently contain hydrogen, a hydrocarbon group having 1 to 50 carbon atoms, a hydroxyl group, a halogen group, an alkoxyl group or an amino group. Represents a hydrocarbon group having 1 to 50 carbon atoms, and R ² and R ³ each independently represent a hydrocarbon group having 1 to 50 carbon atoms including hydrogen, a hydrocarbon group having 1 to 50 carbon atoms, a hydroxyl group or an alkoxyl group. However, the hydrocarbon group may contain an alicyclic structure such as cyclohexyl or an aromatic ring structure such as phenyl or naphthyl.)

As the phosphorus compound used in the present invention, in the above formula (13) ~ (15), R 1, R 4, R 5, R ⁶ is a group having an aromatic ring structure is particularly preferable.

  Examples of the phosphorus compound used in the present invention include, for example, dimethyl methylphosphonate, diphenyl methylphosphonate, dimethyl phenylphosphonate, diethyl phenylphosphonate, diphenyl phenylphosphonate, dimethyl phosphophosphonate, diethyl benzylphosphonate, diphenylphosphinic acid, diphenyl. Examples thereof include methyl phosphinate, phenyl diphenylphosphinate, phenylphosphinic acid, methyl phenylphosphinate, phenyl phenylphosphinate, diphenylphosphine oxide, methyldiphenylphosphine oxide, and triphenylphosphine oxide. Of these, dimethyl phenylphosphonate and diethyl benzylphosphonate are particularly preferred.

  Among the phosphorus compounds described above, it is particularly preferable to use a phosphorus compound having a phenol moiety in the same molecule as the phosphorus compound used in the present invention. The phosphorus compound having a phenol moiety in the same molecule is not particularly limited as long as it is a phosphorus compound having a phenol structure. The use of one or more compounds selected from the group consisting of a compound, a phosphonous acid compound, a phosphinic acid compound, and a phosphine compound is preferred because the effect of improving the catalytic activity is great. Among these, the use of a phosphonic acid compound having one or two or more phenol moieties in the same molecule is particularly preferable because the effect of improving catalytic activity is particularly large.

  Moreover, as a phosphorus compound which has the phenol part used by this invention in the same molecule, since catalyst activity improves especially, it is preferable to use the compound represented by the following general formula (16)-(18).

(In the formulas (16) to (18), R ¹ is a hydrocarbon group having 1 to 50 carbon atoms including a phenol part, a substituent such as a hydroxyl group, a halogen group, an alkoxyl group, or an amino group, and a carbon number 1 including a phenol part. R ⁴ , R ⁵ and R ⁶ each independently represents hydrogen, a hydrocarbon group having 1 to 50 carbon atoms, a carbon containing a substituent such as a hydroxyl group, a halogen group, an alkoxyl group or an amino group. Represents a hydrocarbon group having 1 to 50. R ² and R ³ each independently represent hydrogen, a hydrocarbon having 1 to 50 carbon atoms containing a substituent such as a hydrocarbon group having 1 to 50 carbon atoms, a hydroxyl group or an alkoxyl group. However, the hydrocarbon group may contain a branched structure, an alicyclic structure such as cyclohexyl, or an aromatic ring structure such as phenyl or naphthyl, and the ends of R ² and R ⁴ may be bonded to each other. .)

  Examples of the phosphorus compound having a phenol moiety used in the present invention in the same molecule include p-hydroxyphenylphosphonic acid, dimethyl p-hydroxyphenylphosphonate, diethyl p-hydroxyphenylphosphonate, and diphenyl p-hydroxyphenylphosphonate. Bis (p-hydroxyphenyl) phosphinic acid, methyl bis (p-hydroxyphenyl) phosphinate, phenyl bis (p-hydroxyphenyl) phosphinate, p-hydroxyphenylphenylphosphinic acid, methyl p-hydroxyphenylphenylphosphinate, p-hydroxyphenylphenylphosphinic acid phenyl, p-hydroxyphenylphosphinic acid, p-hydroxyphenylphosphinic acid methyl, p-hydroxyphenylphosphinic acid phenyl, bis (p- Rokishifeniru) phosphine oxide, tris (p- hydroxyphenyl) phosphine oxide, bis (p- hydroxyphenyl) methyl phosphine oxide, and the following equation (19), and the like compounds represented by - (22). Among these, a compound represented by the following formula (21) and dimethyl p-hydroxyphenylphosphonate are particularly preferable.

As a compound represented by the above formula (21), SANKO-220 (manufactured by Sanko Co., Ltd.) can be used.

By adding a phosphorus compound having these phenol moieties in the same molecule during the polymerization of the polyester, the catalytic activity of the polycondensation catalyst is improved and the thermal stability of the polymerized polyester is also improved.

Among the phosphorus compounds described above, in the present invention, it is particularly preferable to use a metal salt compound of phosphorus as the phosphorus compound. The metal salt compound of phosphorus is not particularly limited as long as it is a metal salt of a phosphorus compound. However, the use of a metal salt of a phosphonic acid compound is preferable because the effect of improving catalytic activity is great. Examples of the metal salt of the phosphorus compound include a monometal salt, a dimetal salt, and a trimetal salt.

Further, among the above-described phosphorus compounds, when the metal part of the metal salt is selected from Li, Na, K, Be, Mg, Sr, Ba, Mn, Ni, Cu, and Zn, the catalytic activity is improved. Is preferable. Of these, Li, Na, and Mg are particularly preferable.

  As the phosphorus metal salt compound used in the present invention, it is preferable to use at least one selected from the compounds represented by the following general formula (23) because the effect of improving the catalytic activity is great.

(In formula (23), R ¹ represents hydrogen, a hydrocarbon group having 1 to 50 carbon atoms, a hydroxyl group, a halogen group, an alkoxyl group, or an amino group, and a hydrocarbon group having 1 to 50 carbon atoms. R ² represents Represents a hydrocarbon group having 1 to 50 carbon atoms including hydrogen, a hydrocarbon group having 1 to 50 carbon atoms, a hydroxyl group or an alkoxyl group, and R ³ represents hydrogen, a hydrocarbon group having 1 to 50 carbon atoms, a hydroxyl group or an alkoxyl group. Or a hydrocarbon group having 1 to 50 carbon atoms including carbonyl, l is an integer of 1 or more, m is 0 or an integer of 1 or more, and l + m is 4 or less, M is (l + m) (N represents an integer of 1 or more. The hydrocarbon group may contain an alicyclic structure such as cyclohexyl, a branched structure, or an aromatic ring structure such as phenyl or naphthyl.)

Examples of R ¹ include phenyl, 1-naphthyl, 2-naphthyl, 9-anthryl, 4-biphenyl, 2-biphenyl, and the like. Examples of R ² include hydrogen, methyl group, ethyl group, propyl group, isopropyl group, n-butyl group, sec-butyl group, tert-butyl group, long-chain aliphatic group, phenyl group, naphthyl group, substituted phenyl and naphthyl, and a group defined as -CH ₂ CH ₂ OH and the like. Examples of R ³ O ⁻ include hydroxide ions, alcoholate ions, acetate ions, and acetylacetone ions.

  Among the compounds represented by the general formula (23), it is preferable to use at least one selected from the compounds represented by the following general formula (24).

(In formula (24), R ¹ represents hydrogen, a hydrocarbon group having 1 to 50 carbon atoms, a hydroxyl group, a halogen group, an alkoxyl group, or an amino group, and a hydrocarbon group having 1 to 50 carbon atoms. R ³ represents Hydrogen, a hydrocarbon group having 1 to 50 carbon atoms, a hydroxyl group or an alkoxyl group, or a hydrocarbon group having 1 to 50 carbon atoms including carbonyl, l is an integer of 1 or more, m is 0 or an integer of 1 or more, l + m is 4 or less, M represents a (l + m) -valent metal cation, and the hydrocarbon group may contain an alicyclic structure such as cyclohexyl or a branched structure, or an aromatic ring structure such as phenyl or naphthyl. Good.)

Examples of R ¹ include phenyl, 1-naphthyl, 2-naphthyl, 9-anthryl, 4-biphenyl, 2-biphenyl, and the like. Examples of R ³ O ⁻ include hydroxide ions, alcoholate ions, acetate ions, and acetylacetone ions.

  Among the phosphorus compounds described above, the use of a compound having an aromatic ring structure is preferable because the effect of improving the catalytic activity is great.

Among the above formulas (24), it is preferable that M is selected from Li, Na, K, Be, Mg, Sr, Ba, Mn, Ni, Cu, and Zn because the effect of improving the catalytic activity is large. Of these, Li, Na, and Mg are particularly preferable.

Examples of the metal salt compound of phosphorus used in the present invention include lithium [ethyl (1-naphthyl) methylphosphonate], sodium [ethyl (1-naphthyl) methylphosphonate], magnesium bis [ethyl (1-naphthyl) methylphosphonate], Potassium [(2-naphthyl) methylphosphonate ethyl], magnesium bis [(2-naphthyl) methylphosphonate ethyl], lithium [benzylphosphonate ethyl], sodium [benzylphosphonate ethyl], magnesium bis [benzylphosphonate ethyl], Beryllium bis [benzyl phosphonate], strontium bis [benzyl phosphonate], manganese bis [ethyl benzyl phosphonate], sodium benzyl phosphonate, magnesium bis [benzyl phosphonate], sodium [( -Anthryl) methylphosphonate ethyl], magnesium bis [(9-anthryl) methylphosphonate ethyl], sodium [ethyl 4-hydroxybenzylphosphonate], magnesium bis [4-hydroxybenzylphosphonate ethyl], sodium [4-chlorobenzyl] Phenyl phosphonate], magnesium bis [4-chlorobenzylphosphonate ethyl], sodium [methyl 4-aminobenzylphosphonate], magnesium bis [4-aminobenzylphosphonate methyl], sodium phenylphosphonate, magnesium bis [phenylphosphone] Acid ethyl], zinc bis [ethyl phenylphosphonate] and the like. Among these, lithium [ethyl (1-naphthyl) methylphosphonate], sodium [ethyl (1-naphthyl) methylphosphonate], magnesium bis [ethyl (1-naphthyl) methylphosphonate], lithium [ethyl benzylphosphonate], Sodium [ethyl benzylphosphonate], magnesium bis [ethyl benzylphosphonate], sodium benzylphosphonate and magnesium bis [benzylphosphonic acid] are particularly preferred.

  Among the phosphorus compounds described above, in the present invention, as the phosphorus compound, it is particularly preferable to use at least one selected from a metal salt compound of a specific phosphorus represented by the following general formula (25).

(In the formula (25), R ¹ and R ² each independently represents hydrogen and a hydrocarbon group having 1 to 30 carbon atoms. R ³ represents hydrogen, a hydrocarbon group having 1 to 50 carbon atoms, a hydroxyl group or an alkoxyl. R ⁴ represents a hydrocarbon group having 1 to 50 carbon atoms, including hydrogen, a hydrocarbon group having 1 to 50 carbon atoms, a hydroxyl group, an alkoxyl group, or a carbonyl group. Examples of R ⁴ O ⁻ include hydroxide ion, alcoholate ion, acetate ion, acetylacetone ion, etc. l represents an integer of 1 or more, m represents 0 or an integer of 1 or more, and l + m represents 4 M represents an (l + m) -valent metal cation, n represents an integer of 1 or more, and the hydrocarbon group represents an alicyclic structure such as cyclohexyl or a branched structure, or an aromatic ring structure such as phenyl or naphthyl. May be included.)

  Among these, it is preferable to use at least one selected from compounds represented by the following general formula (26).

(In formula (26), M ^{n +} represents an n-valent metal cation. N represents 1, 2, 3 or 4.)

Among the above formulas (25) or (26), when M is selected from Li, Na, K, Be, Mg, Sr, Ba, Mn, Ni, Cu, Zn, the effect of improving the catalytic activity is obtained. Largely preferred. Of these, Li, Na, and Mg are particularly preferable.

Specific phosphorus metal salt compounds used in the present invention include lithium [ethyl 3,5-di-tert-butyl-4-hydroxybenzylphosphonate], sodium [3,5-di-tert-butyl-4-]. Ethyl hydroxybenzylphosphonate], sodium [3,5-di-tert-butyl-4-hydroxybenzylphosphonic acid], potassium [ethyl 3,5-di-tert-butyl-4-hydroxybenzylphosphonate], magnesium bis [Ethyl 3,5-di-tert-butyl-4-hydroxybenzylphosphonate], magnesium bis [3,5-di-tert-butyl-4-hydroxybenzylphosphonic acid], beryllium bis [3,5-di- tert-butyl-4-hydroxybenzylphosphonate methyl], strontium bis [3,5-di-tert-butyl-4-hydroxybenzylphosphonate ethyl], barium bis [3,5-di -Tert-butyl-4-hydroxybenzylphosphonate phenyl], manganese bis [3,5-di-tert-butyl-4-hydroxybenzylphosphonate ethyl], nickel bis [3,5-di-tert-butyl-4] -Ethyl ethyl hydroxybenzylphosphonate], copper bis [ethyl 3,5-di-tert-butyl-4-hydroxybenzylphosphonate], zinc bis [3,5-di-tert-butyl-4-hydroxybenzylphosphonate] ] Etc. are mentioned. Among these, lithium [ethyl 3,5-di-tert-butyl-4-hydroxybenzylphosphonate], sodium [ethyl 3,5-di-tert-butyl-4-hydroxybenzylphosphonate], magnesium bis [ Ethyl 3,5-di-tert-butyl-4-hydroxybenzylphosphonate] is particularly preferred.

  Among the phosphorus compounds described above, in the present invention, it is particularly preferable to use a phosphorus compound having at least one P—OH bond as the phosphorus compound. The phosphorus compound having at least one P—OH bond is not particularly limited as long as it is a phosphorus compound having at least one P—OH in the molecule. Among these phosphorus compounds, the use of a phosphonic acid compound having at least one P—OH bond is preferable because the effect of improving the catalytic activity is great.

  Among the phosphorus compounds described above, the use of a compound having an aromatic ring structure is preferable because the effect of improving the catalytic activity is great.

  As the phosphorus compound having at least one P—OH bond used in the present invention, it is preferable to use at least one selected from compounds represented by the following general formula (27) because the effect of improving the catalytic activity is great.

(In formula (27), R ¹ represents hydrogen, a hydrocarbon group having 1 to 50 carbon atoms, a hydroxyl group, a halogen group, an alkoxyl group, or an amino group, and a hydrocarbon group having 1 to 50 carbon atoms. R ² represents Represents a hydrocarbon group having 1 to 50 carbon atoms, including hydrogen, a hydrocarbon group having 1 to 50 carbon atoms, a hydroxyl group or an alkoxyl group, n represents an integer of 1 or more, and the hydrocarbon group represents an alicyclic structure such as cyclohexyl, It may contain a branched structure or an aromatic ring structure such as phenyl or naphthyl.)

Examples of R ¹ include phenyl, 1-naphthyl, 2-naphthyl, 9-anthryl, 4-biphenyl, 2-biphenyl, and the like. Examples of R ² include hydrogen, methyl group, ethyl group, propyl group, isopropyl group, n-butyl group, sec-butyl group, tert-butyl group, long-chain aliphatic group, phenyl group, naphthyl group, substituted phenyl and naphthyl, and a group defined as -CH ₂ CH ₂ OH and the like.

  Among the phosphorus compounds described above, the use of a compound having an aromatic ring structure is preferable because the effect of improving the catalytic activity is great.

Examples of the phosphorus compound having at least one P-OH bond used in the present invention include (1-naphthyl) methylphosphonic acid ethyl, (1-naphthyl) methylphosphonic acid, (2-naphthyl) methylphosphonic acid ethyl, benzylphosphonic acid ethyl, Benzylphosphonic acid, ethyl (9-anthryl) methylphosphonate, ethyl 4-hydroxybenzylphosphonate, ethyl 2-methylbenzylphosphonate, phenyl 4-chlorobenzylphosphonate, methyl 4-aminobenzylphosphonate, 4-methoxybenzylphosphone Examples include ethyl acid. Of these, ethyl (1-naphthyl) methylphosphonate and ethyl benzylphosphonate are particularly preferred.

  Among the phosphorus compounds described above, in the present invention, it is particularly preferable to use a specific phosphorus compound having at least one P—OH bond as the phosphorus compound. The specific phosphorus compound having at least one P—OH bond refers to at least one compound selected from compounds represented by the following general formula (28).

(In the formula (28), R ¹ and R ² each independently represent hydrogen and a hydrocarbon group having 1 to 30 carbon atoms. R ³ represents hydrogen, a hydrocarbon group having 1 to 50 carbon atoms, a hydroxyl group or an alkoxyl. Represents a hydrocarbon group containing 1 to 50 carbon atoms, and n represents an integer equal to or greater than 1. The hydrocarbon group includes an alicyclic structure such as cyclohexyl, a branched structure, and an aromatic ring structure such as phenyl or naphthyl. May be.)

  Among these, it is preferable to use at least one selected from compounds represented by the following general formula (29).

(In the formula (29), R ³ represents hydrogen, a hydrocarbon group having 1 to 50 carbon atoms, a hydroxyl group or an alkoxyl group containing an alkoxyl group. The hydrocarbon group is an alicyclic ring such as cyclohexyl. It may contain a structure, a branched structure, or an aromatic ring structure such as phenyl or naphthyl.)

Examples of R ³ include hydrogen, methyl group, ethyl group, propyl group, isopropyl group, n-butyl group, sec-butyl group, tert-butyl group, long-chain aliphatic group, phenyl group, naphthyl group, substituted phenyl and naphthyl, and a group defined as -CH ₂ CH ₂ OH and the like.

Specific phosphorus compounds having at least one P—OH bond used in the present invention include ethyl 3,5-di-tert-butyl-4-hydroxybenzylphosphonate, 3,5-di-tert-butyl-4. -Methyl hydroxybenzylphosphonate, isopropyl 3,5-di-tert-butyl-4-hydroxybenzylphosphonate, phenyl 3,5-di-tert-butyl-4-hydroxybenzylphosphonate, 3,5-di-tert -Octadecyl butyl-4-hydroxybenzylphosphonate, 3,5-di-tert-butyl-4-hydroxybenzylphosphonic acid and the like. Of these, ethyl 3,5-di-tert-butyl-4-hydroxybenzylphosphonate and methyl 3,5-di-tert-butyl-4-hydroxybenzylphosphonate are particularly preferred.

  As a preferable phosphorus compound used by this invention, the phosphorus compound represented by Chemical formula (30) is mentioned.

(In the formula (30), R ¹ represents a hydrocarbon group having ¹ to 49 carbon atoms, or a hydrocarbon group having ¹ to 49 carbon atoms including a hydroxyl group, a halogen group, an alkoxyl group, or an amino group, and R ² , R ³ Each independently represents a hydrocarbon group having 1 to 50 carbon atoms including hydrogen, a hydrocarbon group having 1 to 50 carbon atoms, a hydroxyl group or an alkoxyl group, and the hydrocarbon group includes an alicyclic structure, a branched structure or an aromatic ring structure. You may go out.)

More preferably, at least one of R ¹ , R ² and R ^{3 in} the chemical formula (30) is a compound containing an aromatic ring structure.

  Specific examples of these phosphorus compounds are shown below.

  Moreover, since the phosphorus compound used by this invention has a large molecular weight, since an effect is hard to be distilled off at the time of superposition | polymerization, it is large and preferable.

  Among the phosphorus compounds described above, in the present invention, it is preferable to use at least one phosphorus compound selected from the specific phosphorus compounds represented by the following general formula (37) as the phosphorus compound.

(In the above formula (37), R ¹ and R ² each independently represent hydrogen and a hydrocarbon group having 1 to 30 carbon atoms. R ³ and R ⁴ are each independently hydrogen and hydrocarbon having 1 to 50 carbon atoms. Represents a hydrocarbon group having 1 to 50 carbon atoms including a group, a hydroxyl group or an alkoxyl group, n represents an integer of 1 or more, and the hydrocarbon group represents an alicyclic structure such as cyclohexyl, a branched structure, or an aromatic ring such as phenyl or naphthyl. May contain structure.)

  Among the above general formula (37), it is preferable to use at least one selected from the compounds represented by the following general formula (38) because the effect of improving the catalytic activity is high.

(In said formula (38), R < ³ >, R < ⁴ > represents a C1-C50 hydrocarbon group containing hydrogen, a C1-C50 hydrocarbon group, a hydroxyl group, or an alkoxyl group each independently. Hydrocarbon group. May contain an alicyclic structure such as cyclohexyl, a branched structure, or an aromatic ring structure such as phenyl or naphthyl.)

Examples of R ³ and R ⁴ include short chain aliphatic groups such as hydrogen, methyl and butyl groups, long chain aliphatic groups such as octadecyl, phenyl groups, naphthyl groups, substituted phenyl groups and naphthyl groups. An aromatic group such as a group, a group represented by —CH ₂ CH ₂ OH, and the like.

Specific phosphorus compounds used in the present invention include diisopropyl 3,5-di-tert-butyl-4-hydroxybenzylphosphonate, di-n-3,5-di-tert-butyl-4-hydroxybenzylphosphonate. Examples include butyl, dioctadecyl 3,5-di-tert-butyl-4-hydroxybenzylphosphonate, and diphenyl 3,5-di-tert-butyl-4-hydroxybenzylphosphonate. Of these, dioctadecyl 3,5-di-tert-butyl-4-hydroxybenzylphosphonate and diphenyl 3,5-di-tert-butyl-4-hydroxybenzylphosphonate are particularly preferred.

Among the phosphorus compounds described above, a phosphorus compound particularly preferable to be used in the present invention is at least one phosphorus compound selected from the compounds represented by the chemical formulas (39) and (40).

As the compound represented by the chemical formula (39), Irganox 1222 (manufactured by Ciba Specialty Chemicals) is commercially available, and as the compound represented by the chemical formula (40), Irganox 1425 (Ciba Specialty Chemicals) Are available on the market.

As the aluminum compound or phosphorus compound used in the present invention, it is preferable to use at least one selected from aluminum salts of phosphorus compounds.
The aluminum salt of the phosphorus compound is not particularly limited as long as it is a phosphorus compound having an aluminum portion. However, the use of an aluminum salt of a phosphonic acid compound is preferable because it has a large effect of improving the catalytic activity. Examples of the aluminum salt of the phosphorus compound include a monoaluminum salt, a dialuminum salt, and a trialuminum salt.

  Among the aluminum salts of the phosphorus compounds described above, it is preferable to use a compound having an aromatic ring structure because the effect of improving the catalytic activity is great.

  As the aluminum salt of the phosphorus compound used in the present invention, it is preferable to use at least one selected from compounds represented by the following general formula (41) because the effect of improving the catalytic activity is great.

(In the formula (48), R ¹ represents hydrogen, a hydrocarbon group having 1 to 50 carbon atoms, a hydroxyl group, a halogen group, an alkoxyl group, or an amino group, and a hydrocarbon group having 1 to 50 carbon atoms. R ² represents , Hydrogen, a hydrocarbon group having 1 to 50 carbon atoms, a hydroxyl group or an alkoxyl group, and a hydrocarbon group having 1 to 50 carbon atoms, R ³ represents hydrogen, a hydrocarbon group having 1 to 50 carbon atoms, a hydroxyl group or an alkoxyl group. A hydrocarbon group having 1 to 50 carbon atoms including a group or carbonyl, l is an integer of 1 or more, m is 0 or an integer of 1 or more, l + m is 3. n is an integer of 1 or more (The hydrocarbon group may contain an alicyclic structure such as cyclohexyl, a branched structure, or an aromatic ring structure such as phenyl or naphthyl.)

Examples of R ¹ include phenyl, 1-naphthyl, 2-naphthyl, 9-anthryl, 4-biphenyl, 2-biphenyl, and the like. Examples of R ² include hydrogen, methyl group, ethyl group, propyl group, isopropyl group, n-butyl group, sec-butyl group, tert-butyl group, long-chain aliphatic group, phenyl group, naphthyl group, substituted phenyl and naphthyl, and a group defined as -CH ₂ CH ₂ OH and the like. Examples of R ³ O ⁻ include hydroxide ions, alcoholate ions, ethylene glycolate ions, acetate ions, and acetylacetone ions.

  Examples of the aluminum salt of the phosphorus compound used in the present invention include an aluminum salt of ethyl (1-naphthyl) methylphosphonate, an aluminum salt of (1-naphthyl) methylphosphonic acid, an aluminum salt of ethyl (2-naphthyl) methylphosphonate, and benzylphosphone. Aluminum salt of ethyl acid, aluminum salt of benzylphosphonic acid, aluminum salt of ethyl (9-anthryl) methylphosphonate, aluminum salt of ethyl 4-hydroxybenzylphosphonate, aluminum salt of ethyl 2-methylbenzylphosphonate, 4-chloro Aluminum salt of phenyl benzylphosphonate, aluminum salt of methyl 4-aminobenzylphosphonate, aluminum salt of ethyl 4-methoxybenzylphosphonate, aluminum salt of ethyl phenylphosphonate It is below. Among these, an aluminum salt of ethyl (1-naphthyl) methylphosphonate and an aluminum salt of ethyl benzylphosphonate are particularly preferable.

  As the aluminum compound or phosphorus compound used in the present invention, it is particularly preferable to use at least one selected from aluminum salts of specific phosphorus compounds represented by the following general formula (42).

(In the formula (42), R ¹ and R ² each independently represents hydrogen, a hydrocarbon group having 1 to 30 carbon atoms. R ³ represents hydrogen, a hydrocarbon group having 1 to 50 carbon atoms, a hydroxyl group or an alkoxyl. R ⁴ represents a hydrocarbon group having 1 to 50 carbon atoms, including hydrogen, a hydrocarbon group having 1 to 50 carbon atoms, a hydroxyl group, an alkoxyl group, or a carbonyl group. L is an integer of 1 or more, m is 0 or an integer of 1 or more, and l + m is 3. n is an integer of 1 or more, and the hydrocarbon group is an alicyclic structure such as cyclohexyl or a branched structure. (It may contain an aromatic ring structure such as phenyl or naphthyl.)

  Among these, it is preferable to use at least one selected from compounds represented by the following general formula (43).

(In formula (43), R ³ represents hydrogen, a hydrocarbon group having 1 to 50 carbon atoms, a hydrocarbon group having 1 to 50 carbon atoms including a hydroxyl group or an alkoxyl group. R ⁴ represents hydrogen and 1 carbon atom. Represents a hydrocarbon group having 1 to 50 carbon atoms, including 1 to 50 hydrocarbon group, hydroxyl group or alkoxyl group or carbonyl, l is an integer of 1 or more, m is 0 or an integer of 1 or more, and l + m is 3 The hydrocarbon group may contain an alicyclic structure such as cyclohexyl or a branched structure, or an aromatic ring structure such as phenyl or naphthyl.)

Examples of R ³ include hydrogen, methyl group, ethyl group, propyl group, isopropyl group, n-butyl group, sec-butyl group, tert-butyl group, long-chain aliphatic group, phenyl group, naphthyl group, substituted phenyl and naphthyl, and a group defined as -CH ₂ CH ₂ OH and the like. Examples of R ⁴ O ⁻ include hydroxide ions, alcoholate ions, ethylene glycolate ions, acetate ions, and acetylacetone ions.

Examples of the aluminum salt of the specific phosphorus compound used in the present invention include aluminum salt of ethyl 3,5-di-tert-butyl-4-hydroxybenzylphosphonate, 3,5-di-tert-butyl-4-hydroxybenzyl. Aluminum salt of methyl phosphonate, aluminum salt of isopropyl 3,5-di-tert-butyl-4-hydroxybenzylphosphonate, aluminum salt of phenyl 3,5-di-tert-butyl-4-hydroxybenzylphosphonate, 3 , 5-di-tert-butyl-4-hydroxybenzylphosphonic acid aluminum salt and the like. Of these, the aluminum salt of ethyl 3,5-di-tert-butyl-4-hydroxybenzylphosphonate and the aluminum salt of methyl 3,5-di-tert-butyl-4-hydroxybenzylphosphonate are particularly preferred.

  Examples of the second metal compound that can be used for producing the polyester resin (2) according to the present invention include lithium, sodium, magnesium, calcium, antimony, germanium, tantalum, tungsten, zirconium, hafnium, silicon, iron, nickel, and gallium. And their compounds.

  The use of these compounds in combination within the range of addition amounts that do not cause problems in the product, such as the characteristics, processability, and color tone of the polyester resin (2) as described above, leads to productivity by shortening the polycondensation time. It is effective and preferable in improving.

  The melt polycondensation polyester obtained as described above is, for example, a method in which the melt polyester is extruded into water from the die pores after completion of the melt polycondensation and cut in water, or after the melt polycondensation is finished in the air from the die pores. After being extruded into strands, the chips are formed into columns, spheres, squares or plates by a method of forming chips while cooling with cooling water.

  Moreover, as the cooling water at the time of forming the melt polycondensed polyester into chips, it is preferable to use cooling water satisfying at least one of (1) to (4) of the previous period, and more preferably (1) to (4 It is most preferable to use water that satisfies all of the above.

  The intrinsic viscosity of the polyester resin (2) according to the present invention, particularly the polyester resin (2) in which the main repeating unit is composed of ethylene terephthalate, is 0.55 to 1.50 deciliter / gram, preferably 0.60 to 1. .30 deciliter / gram, more preferably 0.65 to 1.00 deciliter / gram, most preferably 0.70 to 0.85 deciliter / gram. When the intrinsic viscosity of the polyester resin is less than 0.55 deciliter / gram, the mechanical properties of the obtained molded article and the like are poor. In addition, when the intrinsic viscosity of the polyester resin exceeds 1.50 deciliters / gram, a free low molecular weight compound that affects the fragrance retention is caused by the resin temperature becoming high at the time of melting by a molding machine or the like, resulting in severe thermal decomposition. Problems such as an increase and the molded body are colored yellow occur.

  The intrinsic viscosity of the polyester resin (2) according to the present invention, particularly the polyester resin (2) in which the main repeating unit is composed of 1,3-propylene terephthalate, is 0.50 to 1.30 deciliter / Gram, preferably in the range of 0.55 to 1.20 deciliter / gram, more preferably in the range of 0.60 to 1.00 deciliter / gram. When the intrinsic viscosity is less than 0.50 deciliter / gram, there is a problem that the elastic recovery and durability of the obtained molded article are deteriorated. The upper limit of the intrinsic viscosity is 1.30 deciliters / gram. If the upper limit is exceeded, the resin temperature becomes high at the time of molding a molded article, the thermal decomposition becomes severe, the molecular weight decreases drastically, and it is colored yellow. Such problems occur.

  The intrinsic viscosity of the polyester resin (2) according to the present invention, particularly the polyester resin (2) in which the main repeating unit is composed of ethylene-2,6-naphthalate, is 0.40 to 1.00 deciliter / gram, The range is preferably 0.42 to 0.90 deciliter / gram, more preferably 0.45 to 0.80 deciliter / gram. When the IV is less than 0.40 deciliter / gram, the mechanical properties of the obtained molded article are poor. In addition, when it exceeds 1.00 deciliter / gram, it becomes necessary to increase the resin temperature at the time of melting by a molding machine or the like, so that thermal decomposition is accompanied, and free low molecular weight compounds that affect the fragrance retention Problems such as an increase and the molded body are colored yellow occur.

  The content of dialkylene glycol copolymerized with the polyester resin (2) according to the present invention is preferably 0.5 to 7.0 mol%, more preferably 1.% by weight of the glycol component constituting the polyester. It is desirable that it is 0-6.0 mol%, More preferably, it is 1.0-5.0 mol%. When the amount of dialkylene glycol exceeds 7.0 mol%, the thermal stability is deteriorated, the decrease in molecular weight becomes large during molding, and the increase in the content of aldehydes is unfavorable. Further, in order to produce a polyester having a dialkylene glycol content of less than 0.5 mol%, it is necessary to select uneconomical production conditions as transesterification conditions, esterification conditions or polymerization conditions. Do not fit. Here, the dialkylene glycol copolymerized in the polyester, for example, in the case of a polyester whose main structural unit is ethylene terephthalate, is a diethylene glycol by-produced during production from ethylene glycol, which is a glycol. Among them, diethylene glycol (hereinafter abbreviated as DEG) copolymerized with the polyester, and in the case of a polyester having 1,3-propylene terephthalate as a main constituent unit, is glycol 1 Of di (1,3-propylene glycol) (or bis (3-hydroxypropyl) ether) by-produced from 1,3-propylene glycol during production, di (1,3-propylene) copolymerized with the polyester Glycol (hereinafter referred to as DPG).

  The diethylene glycol content copolymerized with the polyester resin (2) according to the present invention, in particular, the polyester whose main repeating unit is composed of ethylene terephthalate is 1.0% of the glycol component constituting the polyester resin. It is desirable that the amount is ˜5.0 mol%, preferably 1.3 to 4.5 mol%, more preferably 1.5 to 4.0 mol%. When the diethylene glycol content exceeds 5.0 mol%, the thermal stability is deteriorated, the decrease in molecular weight during molding is increased, and the increase in the acetaldehyde content is increased. Moreover, when diethylene glycol content is less than 1.0 mol%, the transparency of the obtained molded object worsens.

  In addition, the content of aldehydes such as acetaldehyde in the polyester resin (2) according to the present invention is 50 ppm or less, preferably 30 ppm or less, more preferably 10 ppm or less. When the aldehyde content exceeds 50 ppm, the effect of flavor retention of the contents such as a molded article molded from the polyester resin composition is deteriorated. Further, these lower limits are preferably 0.1 ppb from the viewpoint of production.

  Here, the aldehydes mean that ethylene glycol is a major component of glycol component, such as polyester whose main constituent unit is ethylene terephthalate and polyester whose main constituent unit is ethylene-2,6-naphthalate. In the case of polyester as a component, it is acetaldehyde or formaldehyde, in the case of polyester having 1,3-propylene terephthalate as a main constituent unit, allyl aldehyde, and in the case of polyester having butylene terephthalate as a main constituent unit. Butanal. However, in the case of polyester having butylene terephthalate as the main structural unit, the aldehyde is mostly detected as tetrahydrofuran.

  Further, when the polyester resin (2) according to the present invention is a polyester resin having ethylene terephthalate as a main repeating unit, and the polyester resin composition comprising this is used as a material for a container for low flavor beverages such as mineral water. The acetaldehyde content is desirably 10 ppm or less, preferably 6 ppm or less, and more preferably 4 ppm or less.

  In addition, for the flavor retention of the molded article comprising the polyester resin composition of the present invention, the polyester resin (2) according to the present invention has a free aromatic dicarboxylic acid content derived from the polyester of 20 ppm or less, It is preferable that the polyester resin has a free glycol content of 50 ppm or less, a free aromatic dicarboxylic acid monoglycol ester content of 70 ppm or less, and a free aromatic dicarboxylic acid diglycol ester content of 100 ppm or less.

  As a method for producing such a polyester resin (2), for example, the following method can be employed. That is, a method of solid-phase polymerization of a solution-polymerized polyester prepolymer having IV of 0.40 to 0.60 can be used. Moreover, the method of heat-processing the polyester of predetermined IV on the conditions which IV does not change substantially under inert gas atmosphere or pressure reduction can be used. Moreover, the method of drying polyester at the temperature of 70-180 degreeC under pressure reduction or an inert airflow can be used. Moreover, the method of heat-processing a polyester resin with organic solvents, such as chloroform, can also be used.

  The content of the cyclic ester oligomer of the polyester resin (2) according to the present invention is 70% or less, preferably 60% or less, more preferably 50% of the content of the cyclic ester oligomer contained in the polyester melt polycondensate. Hereinafter, it is particularly preferably 35% or less. The lower limit of the cyclic ester oligomer content is 20% or more, preferably 22% or more, more preferably 25% or more of the cyclic ester oligomer content contained in the melt polycondensate from the viewpoint of economical production. In addition, the content of the cyclic ester oligomer contained in the melt polycondensate of the polyester resin (2) is a free polycondensate present in the polyester resin (2) having a melt polycondensation number average molecular weight of about 5000 or more. The content of the cyclic n-mer having the highest content among several cyclic ester oligomers. In the case where the polyester resin (2) according to the present invention is PET, which is a representative polyester having ethylene terephthalate as a main structural unit, the cyclic n-mer is a cyclic trimer, and melt polycondensation. Since the content of the cyclic trimer of the polyester is about 1.0% by weight, the content of the cyclic trimer is preferably 0.70% by weight or less, more preferably 0.50% by weight or less, and still more preferably Is preferably 0.40% by weight or less. When a heat-resistant hollow molded article or the like is molded from the polyester resin composition of the present invention, heat treatment is performed in a heating mold, but when the cyclic trimer content is 0.70% by weight or more, heating is performed. The adhesion of the oligomer to the mold surface increases rapidly, and the transparency of the obtained hollow molded article is very deteriorated.

  The content of the fine in the polyester resin (2) according to the present invention is 0.1 to 5000 ppm, preferably 0.1 to 3000 ppm, more preferably 0.1 to 1000 ppm, still more preferably 0.1 to 500 ppm, most preferably Preferably it is 0.1-100 ppm. When the blending amount is less than 0.1 ppm, the crystallization rate becomes very slow, and the crystallization of the plug portion of the hollow molded container becomes insufficient, and therefore the shrinkage amount of the plug portion falls within the specified range. It does not fit, and capping is impossible. On the other hand, when it exceeds 5000 ppm, the crystallization speed becomes faster than necessary and the fluctuation of the speed becomes large. Therefore, the degree of crystallinity of the plug portion of the hollow molded body becomes excessive and fluctuated, and therefore the amount of shrinkage of the plug portion does not fall within the specified value range, resulting in poor capping of the plug portion and leakage of contents. Occurs, and the preform for the hollow molded body is whitened, so that normal stretching is impossible. In particular, when the polyester resin (2) is used as a polyester resin for a hollow molded article, the fine content is preferably 0.1 to 500 ppm.

  Further, when the polyester resin (2) according to the present invention is a polyester resin having ethylene terephthalate as a main repeating unit, the haze of a molded product obtained by injection molding thereof is 30% or less, preferably 20% or less. More preferably, it is 10% or less, and the crystallization temperature (Tc1) at the time of temperature rise is 140 to 180 ° C., preferably 145 to 175 ° C., more preferably 150 to 170 ° C.

  The shape of the chip of the polyester resin (2) according to the present invention may be any of a cylinder shape, a square shape, a spherical shape or a flat plate shape. The average particle diameter is usually 1.0 to 4 mm, preferably 1.0 to 3.5 mm, and more preferably 1.0 to 3.0 mm. For example, in the case of a cylinder type, it is practical that the length is about 1.0 to 4 mm and the diameter is about 1.0 to 4 mm. In the case of spherical particles, it is practical that the maximum particle size is 1.1 to 2.0 times the average particle size and the minimum particle size is 0.7 times or more the average particle size. The weight of the chip is practically in the range of 2 to 40 mg / piece. (Polyester resin composition)

  The polyester resin composition of the present invention is a polyester resin composition containing the polyester resin (1) and the polyester resin (2) as main components. The mixing ratio of the polyester resin (1) and the polyester resin (2) constituting the polyester resin composition of the present invention is 0.01 weight of the polyester resin (1) with respect to 100 parts by weight of the polyester resin (2). Parts to 10 parts by weight are preferred. When the blending amount of the polyester resin (1) is less than 0.01 parts by weight, the polycondensation catalyst contained in the polyester resin (2) cannot be sufficiently deactivated, and aldehydes of the obtained molded product The content of is extremely increased, which affects the flavor retention and becomes a problem. In addition, the cyclic ester oligomer content of the molded product becomes very large, and the mold contamination during continuous molding becomes severe. For this reason, the problem that the molded object excellent in transparency cannot be obtained arises. Moreover, when the compounding quantity of the said polyester resin (1) exceeds 10 weight part, the problem that the heat resistance of the obtained molded object worsens or it is colored yellow and the commercial value falls arises.

  The polyester resin (1) and the polyester resin (2) preferably have substantially the same resin composition. Here, “substantially the same” means that the difference in composition is 10 mol% or less, preferably 8 mol% or less, more preferably 6 mol% or less, still more preferably 4 mol% or less, particularly preferably 3 mol% or less. Preferably it is 2 mol% or less. In the case of dialkylene glycol derived from alkylene glycol used in polyester resin (1) and polyester resin (2), the difference in composition is 15 mol% or less, preferably 12 mol% or less, more preferably 10 mol% or less, More preferably, it may be 8 mol% or less, particularly preferably 6 mol% or less, and most preferably 5 mol% or less.

  The content of aldehydes in the polyester resin composition of the present invention is 50 ppm or less, preferably 30 ppm or less, more preferably 10 ppm or less, and further preferably 5 ppm or less. When the content of aldehydes is 50 ppm or more, the flavor and odor of contents such as containers molded from this polyester resin composition are deteriorated. In particular, when the polyester resin according to the present invention is a polyester resin in which the main repeating unit is composed of ethylene terephthalate, the polyester resin composition comprising this is used as a material for containers for low flavor beverages such as mineral water. The content of aldehydes in the polyester resin composition is desirably 10 ppm or less, preferably 8 ppm or less, more preferably 6 ppm or less, and most preferably 5 ppm or less.

When the polyester resin (2) according to the present invention is a polyester resin in which the main repeating unit is composed of ethylene terephthalate, the content of the cyclic trimer of the polyester resin composition of the present invention is 0.70 weight. % Or less, preferably 0.60% by weight or less, more preferably 0.50% by weight or less. When molding a heat-resistant molded article or the like from the polyester resin composition of the present invention, heat treatment is performed in a heating mold or the like. If the content of the cyclic trimer exceeds 0.70% by weight, heating is performed. The adhesion of the oligomer to the mold surface increases rapidly, and the transparency of the resulting molded product is very deteriorated. In particular, in the case of a heat-resistant hollow molded article, the content of the cyclic trimer is desirably 0.40% by weight or less.
It is desirable that the 5 mm-thick molded product obtained by injection molding the polyester resin composition of the present invention has a haze of 30% or less, preferably 25% or less, more preferably 20% or less. In particular, when the polyester resin composition of the present invention is used for a hollow molded article, the haze is preferably 15% or less, and when used for a heat-resistant hollow molded article, the haze is preferably 10% or less. When the haze of the molded body exceeds 30%, the transparency of the obtained molded body is deteriorated, which causes a problem and the commercial value is lost.

  When the polyester is a polyester having ethylene terephthalate as a main structural unit, the crystallization temperature at the time of temperature rise of a test piece from a molded product having a thickness of 2 mm obtained by injection molding the polyester resin composition of the present invention. (Hereinafter referred to as “Tc1”) is in the range of 140 to 180 ° C., preferably in the range of 145 to 175 ° C., and more preferably in the range of 150 to 170 ° C. When Tc1 exceeds 180 ° C., the heating crystallization rate becomes very slow, the crystallization of the hollow molded body plug portion becomes insufficient, and the problem of leakage of contents occurs. On the other hand, when Tc1 is less than 140 ° C., the transparency of the hollow molded article is lowered, which causes a problem.

  The polyester resin composition of the present invention can be obtained by mixing the polyester resin (1) and the polyester resin (2) by a conventionally known method. For example, the polyester resin (1) and the polyester resin (2) are dry blended with a tumbler, V-type blender, Henschel mixer, etc., and the dry blended mixture is a single screw extruder, twin screw extruder, kneader For example, there may be mentioned a method of melt-mixing one or more times by, for example, a method of solid-phase polymerization of the molten mixture under a high vacuum or an inert gas atmosphere if necessary.

  In order to prevent the mixing ratio from fluctuating at the time of mixing or molding, the chip shape and grain weight of the polyester resin (1) and the polyester resin (2) must be substantially the same.

  The polyester resin composition of the present invention may be blended with at least one resin selected from the group consisting of polyolefin resin, polyamide resin, polyacetal resin, and polybutylene terephthalate resin in an amount of 0.1 ppb to 1000 ppm. Good. The blending ratio of the thermoplastic resin such as the polyolefin resin in the polyester resin composition of the present invention is 0.1 ppb to 1000 ppm, preferably 0.3 ppb to 100 ppm, more preferably 0.5 ppb to 1 ppm, and still more preferably 0. .5 ppb to 45 pbb. When the blending amount is less than 0.1 ppb, the crystallization speed becomes very slow and the crystallization of the plug part of the hollow molded body becomes insufficient. Therefore, if the cycle time is shortened, the shrinkage amount of the plug part is specified. Since it does not fall within the value range, capping defects occur, and the heat-fixed mold for forming heat-resistant hollow molded products is heavily soiled. When trying to obtain a transparent hollow molded product, the mold is frequently cleaned. There must be. If it exceeds 1000 ppm, the crystallization speed will be high, and the crystallization of the plug part of the hollow molded body will be excessive, and the shrinkage amount of the plug part will not fall within the specified value range, resulting in capping failure. Leakage occurs, and the preform for the hollow molded body is whitened, so that normal stretching is impossible. Also, in the case of a sheet-like material, if it exceeds 1000 ppm, the transparency is very poor, the stretchability is also impaired, and normal stretching is impossible, and only a stretched film with large thickness spots and poor transparency is obtained. I can't.

Examples of the polyolefin resin blended in the polyester resin composition of the present invention include polyethylene resins, polypropylene resins, and α-olefin resins. These resins may be crystalline or amorphous.
As the polyamide resin blended in the polyester resin composition of the present invention, nylon 4, nylon 6, nylon 7, nylon 8, nylon 9, nylon 11, nylon 12, nylon 66, nylon 69, nylon 610, nylon 611, nylon 612, nylon 6T, nylon 6I, nylon MXD6, nylon 6 / MXD6, nylon MXD6 / MXDI, nylon 6/66, nylon 6/610, nylon 6/12, nylon 6 / 6T, nylon 6I / 6T, and the like. These resins may be crystalline or amorphous.

  In addition, the production of a polyester resin composition containing a thermoplastic resin such as the polyolefin resin can be carried out by directly adding the thermoplastic resin to the polyester resin (2) so that its content falls within the above range. In addition to the method of adding a conventional method such as a method of adding and melting and kneading as a master batch, the thermoplastic resin is used in the production stage of the polyester resin (2), for example, at the time of melt polycondensation, immediately after melt polycondensation, Immediately after pre-crystallization, at the time of solid-phase polymerization, immediately after solid-phase polymerization, or until it reaches the molding stage after finishing the production stage, etc. Or after mixing by the method of making it contact with the said thermoplastic resin member under the flow conditions of the chip | tip of a polyester resin (2), the method of melt-kneading etc. can also be used.

When the polyester resin (2) according to the present invention is a polyester resin in which the main repeating unit is composed of ethylene terephthalate, the intrinsic viscosity of the molded body composed of the polyester resin composition of the present invention is 0.55 to 1.50. It is preferably deciliter / gram, more preferably 0.58 to 1.20 deciliter / gram.
In the case where the polyester resin (2) according to the present invention is a polyester resin in which the main repeating unit is composed of ethylene terephthalate, the acetaldehyde content of the molded body composed of the polyester resin composition of the present invention is preferably 50 ppm or less, preferably Is 30 ppm or less, more preferably 25 ppm or less, and still more preferably 18 ppm or less.

  The polyester resin composition of the present invention is formed by molding a hollow molded body, a tray, a biaxially stretched film or other packaging material, a metal can coating film, a fiber including a monofilament, and the like using a commonly used melt molding method. Alternatively, a coating coated on another substrate can be formed by a melt extrusion method. Moreover, the polyester resin composition of this invention can be used also as 1 component layers, such as a multilayer molded object and a multilayer film.

  The sheet-like material comprising the polyester composition of the present invention can be produced by a means known per se. For example, it can be manufactured using a general sheet forming machine equipped with an extruder and a die.

  Further, the sheet-like material can be formed into a cup shape or a tray shape by pressure forming or vacuum forming. Moreover, the polyester molding from the polyester composition of this invention can be used also for the use of the tray-shaped container for cooking food with a microwave oven and / or an oven range, or heating frozen food. . In this case, after the sheet-like material is formed into a tray shape, it is thermally crystallized to improve heat resistance.

  Moreover, the polyester composition of this invention can be used also as one component layer which took the form of the film form or the coating-film form in composite molded objects, such as a laminated molded object and a laminated film. In particular, it is used for manufacturing containers and the like in the form of a laminate with PET. Examples of laminated molded products include a two-layer structure composed of two layers of an outer layer made of the polyester composition of the present invention and an inner layer of PET, or composed of two layers of an inner layer made of the polyester composition of the present invention and an outer layer of PET. A molded article having a two-layer structure, a three-layer structure composed of an intermediate layer containing the polyester composition of the present invention and an outer layer and an innermost layer of PET, or an intermediate layer of the outer layer and innermost layer containing the polyester composition of the present invention Examples include a three-layered molded body composed of layers, a five-layered molded body composed of an intermediate layer containing the polyester composition of the present invention, an innermost layer of PET, a central layer, and an innermost layer. In the PET layer, other gas barrier resins, ultraviolet blocking resins, heat resistant resins, recovered products from used polyethylene terephthalate bottles, and the like can be mixed and used at an appropriate ratio.

  Other examples of the laminated molded body include a laminated molded body with a resin other than polyester such as polyolefin, and a laminated molded body with a different type of substrate such as paper or a metal plate.

  There is no restriction | limiting in particular in the thickness of the said laminated molded object, and the thickness of each layer. The laminated molded body can be used in various shapes such as a sheet-like material, a film-like material, a plate-like material, a hollow body, and a container.

  The laminate can be produced by co-extrusion using a number of extruders corresponding to the type of the resin layer and a multi-layered multi-die, or with a number of injection machines corresponding to the type of the resin layer. It can also be done by co-injection using an injection runner and injection mold.

Another application of the polyester composition of the present invention is a film that is laminated on one or both sides of a laminated metal plate. Examples of the metal plate used include tinplate, tin-free steel, and aluminum.
As a laminating method, a conventionally known method can be applied, and it is not particularly limited, but it is preferable to carry out by a thermal laminating method that can achieve organic solvent-free and can avoid adverse effects on the taste and odor of food products due to the residual solvent. In particular, the thermal laminating method by energization processing of a metal plate is particularly recommended. In the case of double-sided lamination, lamination may be performed simultaneously or sequentially.

  Needless to say, a film can be laminated to a metal plate using an adhesive.

  Moreover, a metal container is obtained by shape | molding using the said laminated metal plate. The method for forming the metal container is not particularly limited. Further, the shape of the metal container is not particularly limited, but is preferably applied to a so-called two-piece can produced by a molding process such as drawing, drawing and ironing, and stretch draw molding. The present invention can also be applied to a so-called three-piece can in which a top cover suitable for filling a food product such as a coffee drink is wrapped to fill the contents.

Below, the concrete manufacturing method about the various uses in the case of PET is demonstrated easily.
In producing a stretched film, the stretching temperature is usually 80 to 130 ° C. Stretching may be uniaxial or biaxial, but biaxial stretching is preferred from the viewpoint of film physical properties. In the case of uniaxial stretching, the stretching ratio is usually 1.1 to 10 times, preferably 1.5 to 8 times. In the case of biaxial stretching, the longitudinal and transverse directions are usually 1.1 to 8 times, respectively. Preferably, it may be performed in a range of 1.5 to 5 times. The vertical / horizontal magnification is usually 0.5 to 2, preferably 0.7 to 1.3. The obtained stretched film can be further heat-set to improve heat resistance and mechanical strength. The heat setting is usually performed under tension at 120 to 240 ° C., preferably 150 to 230 ° C., usually for several seconds to several hours, preferably several tens of seconds to several minutes.

  In producing the hollow molded body, the blow molded from the polyester resin composition of the present invention is stretch blow molded, and an apparatus conventionally used in blow molding of PET can be used. Specifically, for example, once a preform is formed by injection molding or extrusion molding, the plug portion and the bottom portion are processed as they are, and then reheated, and then biaxial stretch blow molding such as hot parison method or cold parison method. The law applies. The molding temperature in this case, specifically, the temperature of each part of the cylinder of the molding machine and the nozzle is usually in the range of 260 to 300 ° C. The stretching temperature is usually 70 to 120 ° C., preferably 90 to 110 ° C., and the stretching ratio is usually 1.5 to 3.5 times in the longitudinal direction and 2 to 5 times in the circumferential direction. The obtained hollow molded body can be used as it is, but in particular in the case of beverages that require hot filling, such as fruit juice beverages and oolong teas, it is generally heat-set in a blow mold and heat resistant. Used to impart sex. The heat setting is usually performed at 100 to 200 ° C., preferably 120 to 180 ° C. for several seconds to several hours, preferably several seconds to several minutes, under tension by compressed air or the like.

  In addition, in order to impart heat resistance to the plug part, the plug part of the preform obtained by injection molding or extrusion molding is crystallized in a far-infrared or near-infrared heater installation oven, or after the bottle is molded The stopper is crystallized with the heater.

The polyester resin composition of the present invention is also used for the production of a stretched hollow molded body by a so-called compression molding method in which a preform obtained by compression molding a melted mass cut after melt extrusion is stretch blow molded. be able to.
The polyester resin composition of the present invention includes, in addition to the above-mentioned added amount of thermoplastic resin, other thermoplastic resins such as gas barrier polyamides such as gas barrier polyesters, ultraviolet absorbing polyesters, and xylylene group-containing polyamides. An appropriate amount of a resin or the like can be blended as necessary within a range that does not impair the effects of the present invention.

  In addition, the polyester resin composition of the present invention includes a known ultraviolet absorber, antioxidant, oxygen scavenger, aldehyde scavenger, a lubricant added from the outside, a lubricant internally precipitated during the reaction, a release agent, if necessary. Various additives such as a mold agent, a nucleating agent, a stabilizer, an antistatic agent, a bluing agent, a dye, and a pigment may be blended.

  In addition, when the polyester resin composition of the present invention is used for a film application, in order to improve handling properties such as slipping property, winding property, and blocking resistance, calcium carbonate, magnesium carbonate, barium carbonate, Inorganic particles such as calcium sulfate, barium sulfate, lithium phosphate, calcium phosphate, and magnesium phosphate, organic salt particles such as calcium oxalate, calcium, barium, zinc, manganese, magnesium, terephthalate, divinylbenzene, styrene, acrylic acid Inactive particles such as crosslinked polymer particles such as methacrylic acid, acrylic acid or a vinyl monomer of methacrylic acid, alone or as a copolymer can be contained.

EXAMPLES Hereinafter, the present invention will be specifically described with reference to examples, but the present invention is not limited to these examples.
The main characteristic value measurement methods will be described below.

(1) Intrinsic viscosity of polyester (hereinafter referred to as “IV”)
It calculated | required from the solution viscosity at 30 degreeC in a 1,1,2,2-tetrachloroethane / phenol (2: 3 weight ratio) mixed solvent.
As a sample for measuring the intrinsic viscosity of the polyester chip, the polyester is frozen and ground for measurement.

(2) Acetaldehyde content of polyester (hereinafter referred to as “AA content”)
Sample / distilled water = 0.2 to 1 g / 2 cc of glass ampoule substituted with nitrogen was sealed and subjected to extraction treatment at 160 ° C for 2 hours. After cooling, acetaldehyde in the extract was subjected to high-sensitivity gas chromatography. The concentration was measured by chromatography and the concentration was expressed in ppm. The said operation is repeated 5 times and let the average value be AA content.

(3) Diethylene glycol content of polyester (hereinafter referred to as [DEG content])
It decomposed | disassembled with methanol and quantified DEG content by the gas chromatography, and represented with the ratio (mol%) with respect to all the glycol components.

(4) Polyester cyclic trimer content (hereinafter referred to as “CT content”)
300 mg of a sample is dissolved in 3 ml of a hexafluoroisopropanol / chloroform mixed solution (volume ratio = 2/3), and further diluted with 30 ml of chloroform. To this is added 15 ml of methanol to precipitate the polymer, followed by filtration. The filtrate was evaporated to dryness, brought to a constant volume with 10 ml of dimethylformamide, and the cyclic trimer was quantified by high performance liquid chromatography.

(5) Cr, Fe metal content analysis sample 1.2g in polyester was put in a platinum crucible, carbonized using an electric heater, and then heated at 550 ° C. overnight using an electric furnace to be incinerated. Next, a solution obtained by dissolving ash in a 1.2 M hydrochloric acid solution was used as a measurement solution, and Cr and Fe elements were measured using IPC emission spectrometry.

(6) Haze (degree%)
A sample was cut from the molded product (thickness 5 mm) of (9) below, and measured with a Nippon Denshoku Co., Ltd. haze meter, model NDH2000.

(7) Crystallization temperature (Tc1) at the time of temperature rise of the compact
Measured with a differential thermal analyzer (DSC) manufactured by Seiko Denshi Kogyo Co., Ltd., RDC-220. 10 mg of a sample from the center of a 2 mm thick plate of the molded plate of (9) below is used. The temperature is raised at a rate of temperature rise of 20 ° C./minute, and the temperature at the top of the crystallization peak observed in the middle is measured to obtain the crystallization temperature at the time of temperature rise (Tc1).

(8) Color b value of molded product The molded product of the following (9) (wall thickness: 4 mm) and the resin prepared in the examples are in accordance with Tokyo Denshoku color difference meter TC-1500MC-88 JIS-Z8722 (Hunter color difference). Measured.
The higher the color b, the greater the degree of coloring.

(9) Molding of Stepped Molding Plate In molding of the stepped molding plate according to this patent description, a polyester chip that has been dried under reduced pressure to a water content of about 50 ppm or less using a vacuum dryer is an injection molding machine M manufactured by Meiki Seisakusho. -150C-DM type injection molding machine having a gate part (G) as shown in FIG. 1 and FIG. 2, 2 mm to 11 mm (A part thickness = 2 mm, B part thickness = 3 mm, C part thickness = 4 mm) A stepped molding plate having a thickness of D part = 5 mm, E part thickness = 10 mm, and F part thickness = 11 mm) was injection molded.

A polyester chip previously dried under reduced pressure using a vacuum dryer DP61 manufactured by Yamato Scientific was used, and a dry inert gas (nitrogen gas) purge was performed in the molding material hopper in order to prevent moisture absorption of the chip during molding.
The plasticizing conditions of the M-150C-DM injection molding machine are as follows: feed screw rotation speed = 70%, screw rotation speed = 120 rpm, back pressure 0.5 MPa, cylinder temperature 45 ° C., 250 ° C. from the bottom of the hopper in order, nozzle The temperature was set at 290 ° C. The injection conditions are 20% for injection speed and holding pressure, and the injection pressure and holding pressure are adjusted so that the weight of the molded product is 146 ± 0.2g. In this case, the holding pressure is 0.5MPa lower than the injection pressure. It was adjusted.

The upper limit of the injection time and pressure holding time is set to 10 seconds and 7 seconds, respectively, and the cooling time is set to 50 seconds. The total cycle time including the time for taking out the molded product is about 75 seconds.
Although the temperature of the mold is always controlled by introducing cooling water having a water temperature of 10 ° C., the mold surface temperature at the time of stable molding is around 22 ° C.

The test plate for evaluating the molded product characteristics was arbitrarily selected from the 11th to 18th shots of the stable molded product after the molding material was introduced and the resin was replaced.
A 2 mm thick plate (part A in FIG. 1) measures the crystallization temperature (Tc1) and acetaldehyde content at elevated temperature, a 4 mm thick plate (part C in FIG. 1) measures the color b value, and 5 mm. A plate having a thickness (D portion in FIG. 1) is used for haze (degree of haze) measurement.

(10) Molding of hollow molded body A preform was molded at a resin temperature of 290 ° C using an M-150C-DM injection molding machine manufactured by Koki Seisakusho using the dried polyester resin and polyester resin composition. The plug portion of this preform was heated and crystallized with a home-made plug portion crystallizer. Next, this preformed body was biaxially stretched and blown at a magnification of about 2.5 times in the longitudinal direction and about 3.8 times in the circumferential direction on an LB-01E molding machine manufactured by CORPOPLAST, and subsequently set at about 150 ° C. The container was heat-set in a mold to form a container (body thickness 0.45 mm) having a capacity of 2000 cc. The stretching temperature was controlled at 100 ° C.

(11) Sensory test Boiled distilled water was put into the hollow container obtained in (10) above, kept for 30 minutes after sealing, and allowed to stand at 55 ° C. for 1 week, and tested for flavor, odor and the like after opening. Use distilled water as a blank for comparison. The sensory test was carried out by 10 panelists according to the following criteria, and the average values were compared.
(Evaluation criteria)

◎: Feel no strange taste or smell ○: Feel a slight difference from the blank △: Feel a difference from the blank ×: Feel a considerable difference from the blank XX: Feel a very large difference from the blank

(Polyester resin (1) -A)
1162 kg of high-purity terephthalic acid and its 2-fold molar amount of ethylene glycol are charged into a heat-medium circulating esterification reactor with a stirrer made of Hastelloy, and 0.3 mol% of triethylamine is added to the acid component, and the pressure is 0.25 MPa. The esterification reaction was carried out for 2 hours while distilling water out of the system at 245 ° C. to obtain a mixture of bis (2-hydroxyethyl) terephthalate and oligomer (hereinafter referred to as BHET mixture) having an esterification rate of 95%. This BHET mixture was transported to a Hastelloy-made polycondensator with a stirrer, and a crystalline germanium dioxide / ethylene glycol solution and a polyester obtained by heating phosphoric acid and ethylene glycol as a polycondensation catalyst to the polyester were obtained respectively. An amount of about 20 ppm and a P residual amount of about 2000 ppm were added. Subsequently, it stirred at 245 degreeC for 10 minutes by the normal pressure in nitrogen atmosphere. Thereafter, while raising the temperature to 245 ° C., the pressure of the reaction system is gradually reduced to 13.3 Pa (0.1 Torr) for 50 minutes to perform the first stage initial polycondensation, and IV is further increased at 275 ° C. and 13.3 Pa. The polycondensation reaction was carried out to about 0.65 deciliter / gram. Subsequent to releasing the pressure, the resin under slight pressure was discharged into cold water in the form of a strand and rapidly cooled, and was converted into a chip with a strand cutter to obtain a cylindrical chip. At the time of chip formation, the resin temperature from the polycondenser outlet to the nozzle pores was about 270 ° C., and the entire amount was chipped within about 30 minutes.
Subsequently, it heat-processed at about 50-150 degreeC with the vacuum dryer immediately, and it processed by the vibration type sieving process and the airflow classification process, and obtained the crystallized polymer. IV is 0.65 deciliter / gram, acetaldehyde content is 48 ppm, DEG content is 4.7 mol%, cyclic trimer content is 7200 ppm, Cr atom content and Fe atom content are each 0.00%. 1 ppm. The characteristics are shown in Table 1.

(Polyester resin (1) -B)
Using an SUS316L heat medium circulating esterification reactor with a stirrer, except that the polycondensation time is shortened, until IV becomes about 0.56 deciliter / gram under the same conditions as for obtaining the polyester resin (1) -A A melt polycondensation reaction was performed.

  After the polyester chip obtained by the melt polycondensation reaction is heat-treated to crystallize the polyester, it is dried at about 100 ° C. to 130 ° C. and then at 150 ° C. in a stationary solid phase polycondensation tower under a nitrogen stream Solid state polymerization at 185 ° C. and IV of 0.72 deciliter / gram, acetaldehyde content of 27 ppm, DEG content of 5.2 mol%, cyclic trimer content of 6200 ppm, Cr atom content of 4 ppm, Fe The atomic content was 10 ppm. The characteristics are shown in Table 1.

(Polyester resin (1) -C)
The polyester resin (1)-, except that a heat medium circulating esterification reactor with a stirrer made of SUS316 was used and antimony trioxide was added as a polycondensation catalyst instead of crystalline germanium dioxide so that the residual amount of Sb was 180 ppm. Polycondensation was carried out in the same manner as in B to obtain a polyester resin with IV = 0.65 deciliter / gram.
This was subjected to a dry crystallization treatment in the same manner as the polyester resin (1) -A. IV was 0.65 deciliter / gram, acetaldehyde content was 55 ppm, DEG content was 5.5 mol%, cyclic trimer content was 6500 ppm, Cr atom content was 8 ppm, Fe atom content was 25 ppm. It was. The characteristics are shown in Table 1.

(Polyester Resin (1) -D) (Production Method of Comparative Example Polyester)
1162 kg of high-purity terephthalic acid and its 2-fold molar amount of ethylene glycol were charged into a SUS304 heating medium circulation type esterification reactor equipped with a stirrer, 0.1 mol% of triethylamine was added to the acid component, and the pressure was 0.25 MPa. The esterification reaction was carried out for 2 hours while distilling water out of the system at 245 ° C. to obtain a mixture of bis (2-hydroxyethyl) terephthalate and oligomer (hereinafter referred to as BHET mixture) having an esterification rate of 95%. This BHET mixture was transported to a polycondensator with a stirrer made of SUS304, and a germanium dioxide / ethylene glycol solution as a polycondensation catalyst and a polyester obtained by heat-treating phosphoric acid and ethylene glycol as a polycondensation catalyst were each left in Ge. An amount of about 20 ppm and a P residual amount of about 2000 ppm were added. Subsequently, it stirred at 245 degreeC for 10 minutes by the normal pressure in nitrogen atmosphere. Thereafter, while raising the temperature to 245 ° C., the pressure of the reaction system is gradually reduced to 13.3 Pa (0.1 Torr) for 50 minutes to perform the first stage initial polycondensation, and IV is further increased at 275 ° C. and 13.3 Pa. The polycondensation reaction was carried out to about 0.65 deciliter / gram. Subsequent to releasing the pressure, the resin under slight pressure was discharged into cold water in the form of a strand and rapidly cooled, and was converted into a chip with a strand cutter to obtain a cylindrical chip. At the time of chip formation, the resin temperature from the polycondenser outlet to the nozzle pores was about 270 ° C., and the entire amount was chipped within about 30 minutes.

  Subsequently, it heat-processed at about 50-150 degreeC with the vacuum dryer immediately, and it processed by the vibration type sieving process and the airflow classification process, and obtained the crystallized polymer. IV was 0.65 deciliter / gram, acetaldehyde content was 49 ppm, DEG content was 6.7 mol%, cyclic trimer content was 7400 ppm, Cr atom content was 18 ppm, and Fe atom content was 35 ppm. It was. The characteristics are shown in Table 2.

(Polyester resin (2) -A)
A slurry of high-purity terephthalic acid and ethyl glycol is continuously supplied to the first esterification reactor containing the reactants in advance, and the average residence is maintained at about 250 ° C. and 0.5 kg / cm ² G under stirring. The reaction was carried out for 3 hours. This reaction product was sent to the second esterification reactor, and the reaction was carried out with stirring at about 260 ° C. and 0.05 kg / cm ² G to a predetermined reactivity. In addition, an ethylene glycol solution of basic aluminum acetate, Irganox 1222 (manufactured by Ciba Specialty Chemicals), and an ethylene glycol solution in which ethylene glycol was previously heated were continuously supplied to the second esterification reactor. The esterification reaction product is continuously fed to the first polycondensation reactor, and is stirred for about 1 hour at about 265 ° C. and 25 torr, and then stirred for about 2 hours at about 265 ° C. and 3 torr. The mixture was further polycondensed at about 275 ° C. and 0.3 to 1 torr with stirring in the final polycondensation reactor. The obtained melt polycondensed PET had an intrinsic viscosity of 0.55 deciliter / gram. The polycondensation reaction product is chipped into a cylinder-shaped chip, followed by crystallization at about 155 ° C. in a nitrogen atmosphere, further preheated to about 200 ° C. in a nitrogen atmosphere, and then sent to a continuous solid state polymerization reactor under a nitrogen atmosphere. Solid state polymerization was carried out at about 207 ° C. After the solid phase polymerization, fines were removed by continuous treatment in a sieving step and a fine removal step.

The obtained PET had an intrinsic viscosity of 0.74 deciliter / gram, an acetaldehyde content of 3.2 ppm, a DEG content of 2.6 mol%, a cyclic trimer content of 0.33 wt%, and a density of 1 400 g / cm ³ . Al residual amount was 20 ppm, P residual amount was 35 ppm, and fine content was about 50 ppm. The characteristics are shown in Table 1.

(Polyester resin (2) -B)
The same method as in the case of the polyester resin (2) -A, except that an ethylene glycol solution of titanium tetrabutoxide, an ethylene glycol solution of magnesium acetate tetrahydrate as a polycondensation catalyst, and an ethylene glycol solution of phosphoric acid as a stabilizer are used. A melt polycondensed PET was obtained. The obtained melt polycondensed PET had an intrinsic viscosity of 0.58 deciliter / gram.

Next, solid phase polymerization was performed in the same manner as in the case of the polyester resin (2) -A.
The obtained PET has an intrinsic viscosity of 0.75 deciliter / gram, an acetaldehyde content of 5.1 ppm, a DEG content of 2.6 mol%, a cyclic trimer content of 3700 ppm, and a density of 1.399 g / cm. It was ³ . Ti residual amount was 3.5 ppm, Mg residual amount was 2 ppm, P residual amount was 7 ppm, and fine content was about 50 ppm. The characteristics are shown in Table 1.

(Polyester resin (2) -C)
A melt polycondensation PET was obtained in the same manner as in the case of the polyester resin (2) -A except that an ethylene glycol solution of antimony trioxide as a polycondensation catalyst and an ethylene glycol solution of phosphoric acid as a stabilizer were used. The obtained melt polycondensed PET had an intrinsic viscosity of 0.57 deciliter / gram. Next, solid phase polymerization was performed in the same manner as in the case of the polyester resin (2) -A.

The obtained PET has an intrinsic viscosity of 0.75 deciliter / gram, an acetaldehyde content of 5.0 ppm, a DEG content of 2.6 mol%, a cyclic trimer content of 3400 ppm, and a density of 1.402 g / cm. It was ³ . The residual amount of Sb was 290 ppm, the residual amount of P was 12 ppm, and the fine content was about 50 ppm. The characteristics are shown in Table 1.

Example 1

  The polyester resin (2) -A, 98 parts by weight, and the catalyst-reused polyester resin (1) -A, 2 parts by weight were mixed in a blender. Thereafter, a stepped molded plate was formed by the method (9), and a bottle that was a hollow formed body was formed by the method (10).

  The haze of the stepped molded plate (5 mm thick) was 6.1%, the acetaldehyde content was 13.8 ppm, the color b value was 0.2, and the sensory test had no problem. Tc1 of the molded plate was as good as 166 ° C., and there was no problem.

(Example 2)
The polyester resin (2) -A, 98 parts by weight, and the catalyst-reused polyester resin (1) -B, 2 parts by weight were mixed in a blender. Thereafter, a stepped molded plate was formed by the method (9), and a bottle that was a hollow formed body was formed by the method (10).

  The haze of the stepped molded plate (5 mm thick) was 6.2%, the acetaldehyde content was 14.0 ppm, the color b value was 0.6, and the sensory test had no problem. The Tc1 of the molded plate was 164 ° C., and there was no problem.

(Example 3)
The polyester resin (2) -B, 98 parts by weight, and the catalyst-reused polyester resin (1) -B, 2 parts by weight were mixed in a blender. Thereafter, a stepped molded plate was formed by the method (9), and a bottle that was a hollow formed body was formed by the method (10).

  The haze of the stepped molded plate (5 mm thick) was 6.3%, the acetaldehyde content was 14.4 ppm, the color b value was 0.8, and the sensory test had no problem. The Tc1 of the molded plate was 169 ° C., and there was no problem.

Example 4
The polyester resin (2) -B, 98 parts by weight, and the catalyst-reused polyester resin (1) -C, 2 parts by weight were mixed in a blender. Thereafter, a stepped molded plate was formed by the method (9), and a bottle that was a hollow formed body was formed by the method (10).

  The haze of the stepped molded plate (5 mm thick) was 6.7%, the acetaldehyde content was 14.7 ppm, the color b value was 1.3, and the sensory test had no problem. Tc1 of the molded plate was 163 ° C., and there was no problem.

(Comparative Example 1)
The polyester resin (2) -A, 98 parts by weight and the polyester resin (1) -D, 2 parts by weight were mixed in a blender. Thereafter, a stepped molded plate was formed by the method (9), and a bottle that was a hollow formed body was formed by the method (10).
The haze of the stepped molded plate (5 mm thick) was 29.5%, Tc1 was 155 ° C., the acetaldehyde content was 29.5 ppm, and the color b value was 4.5. The sensory test was bad as x.

(Comparative Example 2)
The polyester resin (2) -C, 98 parts by weight and polyester resin (1) -D, 2 parts by weight were mixed in a blender. Thereafter, a stepped molded plate was formed by the method (9), and a bottle that was a hollow formed body was formed by the method (10).
The haze of the stepped molded plate (5 mm thickness) was 49.5%, Tc1 was 133 ° C., the acetaldehyde content was 54 ppm, and the color b value was 5.8. The sensory test was XX.

  As mentioned above, although the polyester resin of this invention, the polyester resin composition consisting thereof, and its use were demonstrated based on several Example, this invention is not limited to the structure described in the said Example, Each implementation The configuration can be appropriately changed within a range not departing from the gist, such as appropriately combining the configurations described in the examples.

  The polyester resin of the present invention is a polyester resin that can be used to deactivate the polycondensation catalyst used in the production of polyester and suppress the formation of aldehydes such as acetaldehyde and cyclic ester oligomers during molding. It can be used suitably. In particular, the polyester resin composition of the present invention is excellent in transparency and flavor retention, has no problems such as deterioration of transparency due to mold contamination during continuous molding, and has a hollow molded body excellent in heat-resistant dimensional stability. It is a polyester resin composition that can be produced efficiently, and from this, it is possible to obtain a molded product having the above-mentioned characteristics, which contributes greatly to the industry.

Plan view of the stepped molded plate used in the examples Side view of the stepped molded plate of FIG.

Claims (7)

A polyester resin mainly comprising an aromatic dicarboxylic acid component and a glycol component, and containing a phosphorus compound as a phosphorus atom in an amount of 100 to 10,000 ppm, wherein the Cr atom content (Cr) and the Fe atom content (Fe) are A polyester resin characterized by satisfying A and B.
Cr ≦ 10ppm (A)
Fe ≦ 30ppm (B) The polyester resin according to claim 1, wherein the polycondensation catalyst is at least one selected from the group consisting of an Sb compound and a Ge compound. The polyester resin (1) according to claim 1 or 2 is selected from the group consisting of Al, Ti, Mn, Fe, Co, Zn, Nb, Mo, Cd, In, Sn, Ta and Pb as a polycondensation catalyst. In addition, the polycondensation catalyst of the polyester resin (2) is lost by mixing with a polyester resin (2) mainly containing an aromatic dicarboxylic acid component and a glycol component and containing a compound containing at least one element. A polyester resin with a catalyst lost, characterized in that it can be activated. The polyester resin (1) according to any one of claims 1 to 3, and selected from the group consisting of Al, Ti, Mn, Fe, Co, Zn, Nb, Mo, Cd, In, Sn, Ta and Pb. A polyester comprising a polyester resin (2) mainly comprising an aromatic dicarboxylic acid component and a glycol component, containing a compound containing at least one element and optionally an antimony compound and / or a germanium compound. Resin composition. A polyester molded article obtained by melt-molding the polyester resin composition according to claim 4. The polyester molded body according to claim 5, wherein the polyester molded body is any one of a hollow molded body, a sheet-like material, and a stretched film obtained by stretching the sheet-like material in at least one direction. A coated product obtained by melt-extruding the polyester resin composition according to claim 4 onto a substrate.

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