초록 ▼

The object of the present invention is to provide a high quality polyester resin having high productivity, stability and safety, a catalyst for polyester production with high catalytic activity, a method for producing the polyester resin with the catalyst, a polyester resin obtained with the catalys

The object of the present invention is to provide a high quality polyester resin having high productivity, stability and safety, a catalyst for polyester production with high catalytic activity, a method for producing the polyester resin with the catalyst, a polyester resin obtained with the catalyst, and a hollow molded container having the polyester resin. The polyester resin of the present invention satisfies specific parameters regarding polymerizability, stability, and metal content. The catalyst for polyester production satisfies specific parameters. The catalyst particularly preferably has: (a) a solid titanium-containing compound which has a maximum solubility in ethylene glycol of 1,000 ppm or more in terms of converted titanium amount when dissolved in ethylene glycol with heating at 150째 C., and which has titanium, oxygen, carbon, and hydrogen, and optionally an alkali metal, and has a Ti--O--C bond; and (b) an alkali metal compound, the molar ratio of the alkali metal atoms to the titanium atom in the catalyst being in the range of 20/1 to 0.1/1.

대표청구항 ▼

The invention claimed is: 1. A polyester resin of which the polymerizability parameter satisfies the following formula (A-1), the stability parameter satisfies the following formula (B-1), and the metal content parameter further satisfies the following formula (C-1): description="In-line Formulae

The invention claimed is: 1. A polyester resin of which the polymerizability parameter satisfies the following formula (A-1), the stability parameter satisfies the following formula (B-1), and the metal content parameter further satisfies the following formula (C-1): description="In-line Formulae" end="lead"Vssp≧0.025(dl/g쨌h) (A-1)description="In-line Formulae" end="tail" wherein Vssp is calculated from the intrinsic viscosity of polyester resin, and the intrinsic viscosity of polyester resin after solid polycondensation of this polyester resin at 220째 C. under nitrogen atmosphere for any hours between 2 hours and 12 hours, by the following calculation formula: description="In-line Formulae" end="lead"Vssp=([IV]1-[IV]0 )/Tdescription="In-line Formulae" end="tail" wherein [IV]0 and [IV]1 represent intrinsic viscosities (dl/g) before and after the solid polycondensation, respectively, and T represents solid polycondensation time (h); description="In-line Formulae" end="lead"ΔAA≦7.0 (ppm) (B-1)description="In-line Formulae" end="tail" wherein ΔAA is calculated from the acetaldehyde amount contained originally in the polyester resin, and the acetaldehyde amount contained in a preform obtained by molding this polyester resin with an injection molding machine at a cylinder temperature of 265 to 275째 C. for 26짹1 seconds of a molding cycle, by the following calculation formula: description="In-line Formulae" end="lead"ΔAA=[AA]1-[AA]0description="In-line Formulae" end="tail" wherein [AA]0 and [AA]1 represent acetaldehyde contents (ppm by weight) before and after the molding, respectively; description="In-line Formulae" end="lead"M≦50 (ppm) (C-1)description="In-line Formulae" end="tail" wherein M represents the total amount (ppm by weight) of the metal atoms contained in the polyester resin. 2. The polyester resin as described in claim 1, wherein the polycondensation time further satisfies the following formula (A-2): description="In-line Formulae" end="lead"T≦8 (h) (A-2)description="In-line Formulae" end="tail" wherein T represents solid polycondensation time (h) required for elevating the molecular weight of the polyester resin to attain an intrinsic viscosity of 0.84 dl/g by carrying out solid polycondensation of the polyester resin having an intrinsic viscosity of 0.64 dl/g at 220째 C. under nitrogen atmosphere. 3. The polyester resin as described in claim 1 or 2, wherein the metal content parameter further satisfies the following formula (C-2): description="In-line Formulae" end="lead"HM≦2 (ppm) (C-2)description="In-line Formulae" end="tail" wherein HM represents the total amount (ppm by weight) of the heavy metal atoms contained in the polyester resin. 4. A catalyst for polyester production comprising: (a) a solid titanium-containing compound which comprises titanium, oxygen, carbon, and hydrogen, wherein said solid titanium-containing compound has a Ti--O--C bond, a weight ratio of the titanium atom to carbon atom (Ti/C) is in the range of 50 to 1, and the maximum solubility in ethylene glycol when dissolved in the ethylene glycol at 150째 C. is 1,000 ppm or more in terms of converted titanium atom, and (b) an alkali metal compound, wherein the molar ratio of the alkali metal atoms to the titanium atom in the catalyst being in the range of 20/1 to 0.1/1. 5. The catalyst for polyester production as described in claim 4, wherein the solid titanium-containing compound (a) further contains alkali metal in addition to titanium, oxygen, carbon and hydrogen. 6. A catalyst for polyester production comprising: a solid titanium-containing compound which comprises titanium, oxygen, carbon, hydrogen, and alkali metal, wherein said solid titanium-containing compound has a Ti--O--C bond, a weight ratio of the titanium atom to carbon atom (Ti/C) is in the range of 50 to 1, and the maximum solubility in ethylene glycol when dissolved in the ethylene glycol under heating at 150째 C. is 1,000 ppm or more in terms of converted titanium atom, and the molar ratio of the alkali metal atoms to the titanium atom being in the range of 20/1 to 0.1/1. 7. The catalyst for polyester production as described in any one of claims 4 to 6, wherein the titanium atom content in the solid titanium-containing compound (a) is 5 to 50% by weight and the carbon atom content is 1 to 35% by weight. 8. The catalyst for polyester production as described in claim 4 or 6, wherein the solid titanium-containing compound (a) contains at least one kind of element selected from the group consisting of beryllium, magnesium, calcium, strontium, barium, scandium, yttrium, lanthanum, zirconium, hafnium, vanadium, niobium, tantalum, chrome, molybdenum, tungsten, manganese, iron, ruthenium, cobalt, rhodium, nickel, palladium, copper, zinc, boron, aluminum, gallium, silicon, germanium, tin, antimony and phosphorus in addition to titanium, oxygen, carbon, hydrogen and alkali metal. 9. The catalyst for polyester production as described in claim 4 or 6 wherein the solid titanium-containing compound (a) is a product of contact between hydrolysate of titanium halide or hydrolysate of titanium alkoxide, and polyol. 10. A catalyst for polyester production comprising (I) the catalyst for polyester production as described in claim 4 or 6, and (II) a compound of at least one kind of element selected from the group consisting of beryllium, magnesium, calcium, strontium, barium, boron, aluminum, gallium, manganese, cobalt, zinc, germanium, antimony and phosphorus. 11. The catalyst for polyester production as described in claim 4 or 6, wherein the solid titanium-containing compound (a) is a titanium-containing solution in which the solid titanium-containing compound (a) is dissolved in ethylene glycol-containing solution (c) in an amount of 500 to 100,000 ppm in terms of converted titanium atom. 12. The catalyst for polyester production as described in claim 11, wherein the titanium-containing solution is obtained by adding the alkali metal compound (b) when the solid titanium-containing compound (a) is dissolved in the ethylene glycol-containing solution (c). 13. The catalyst for polyester production as described in claim 11 wherein the titanium-containing solution contains a solubilizing aid in the range of 1 to 50% by weight of, relative to the ethylene glycol-containing solution (c). 14. The catalyst for polyester production as described in claim 13 wherein the solubilizing aid is glycerin or trimethylol propane. 15. The catalyst for polyester production as described in claim 13 wherein the water content of the titanium-containing solution is in the range of 0.05 to 15.0% by weight. 16. The catalyst for polyester production as described in claim 4 or 6 substantially comprising no antimony compound and germanium compound. 17. A method for producing a polyester resin wherein aromatic dicarboxylic acid or an ester-forming derivative thereof and aliphatic diol or an ester-forming derivative thereof are subjected to polycondensation to produce the polyester resin under presence of the catalyst for polyester production as described in claim 4 or 6. 18. A polyester resin prepared by polycondensation of aromatic dicarboxylic acid or an ester-forming derivative thereof and aliphatic diol or an ester-forming derivative thereof under presence of the catalyst for polyester production as described in claim 4 or 6. 19. A polyester resin as described in claim 18, made by solid polycondensation having an intrinsic viscosity of 0.60 dl/g or more. 20. A hollow molded container comprising the polyester resin as described in claim 18.