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Catalyst for polyester production, process for producing polyester using the catalyst, polyester obtained by the process, and uses of the polyester |
| RE40571 |
Catalyst for polyester production, process for producing polyester using the catalyst, polyester obtained by the process, and uses of the polyester
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| Patent Drawings: | |
| Inventor: |
Ohmatsuzawa, et al. |
| Date Issued: |
November 11, 2008 |
| Application: |
10/942,080 |
| Filed: |
September 16, 2004 |
| Inventors: |
Ohmatsuzawa; Takeshi (Tokyo, JP)
Ehara; Fujito (Yamaguchi, JP)
Hori; Hideshi (Yamaguchi, JP)
Toyota; Kazuo (Yamaguchi, JP)
Fukutani; Kenzaburou (Yamaguchi, JP)
Imuta; Junichi (Tokyo, JP)
Shimizu; Akiyoshi (Yamaguchi, JP)
Onogi; Takayuki (Sodegaura, JP)
Noda; Seiji (Shimonoseki, JP)
Sakai; Masayuki (Tokyo, JP)
Hiraoka; Shoji (Yamaguchi, JP)
Nakamachi; Koji (Tokyo, JP)
Tsugawa; Michio (Sodegaura, JP)
Miyazoe; Satoru (Sodegaura, JP)
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| Assignee: |
Mitsui Chemicals, Inc. (Tokyo, JP) |
| Primary Examiner: |
Boykin; Terressa |
| Assistant Examiner: |
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| Attorney Or Agent: |
Birch, Stewart, Kolasch & Birch, LLP. |
| U.S. Class: |
528/279; 524/779; 524/780; 524/781; 524/783; 524/784; 524/785; 524/786; 524/788; 524/789; 528/272; 528/274; 528/277; 528/280; 528/281; 528/282; 528/283; 528/285; 528/286; 528/308; 528/308.1; 528/308.2; 528/308.3 |
| Field Of Search: |
524/274; 524/277; 524/279; 524/280; 524/281; 524/282; 524/779; 524/780; 524/781; 524/782; 524/783; 524/784; 524/785; 524/786; 524/788; 524/789; 528/283; 528/285; 528/286; 528/308; 528/308.1; 528/308.2; 528/308.3 |
| International Class: |
C08G 63/82 |
| U.S Patent Documents: |
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| Foreign Patent Documents: |
455290; 655 938; 0 389 948; 0 854 175; 0 867 458; 1179356; 43-18609; 47-26597; 48-000892; 49007356; 49011754; 49 011754; 50-8888; 50-34092; 50034092; 50-156595; 51-37187; 51037187; 51-58495; 51058495; 51-19477; 52-57291; 53-24392; 55-13715; 55-13715; 55-003426; 55-23136; 55-023136; 58-120633; 59-25815; 59-30854; 59-219328; 62-199648; 5-43677; 5-97990; 6-3498050; 64920; 08-020638; 8-41182; 8-99354; 08-208822; 8-283393; 8-283393; 8-283394; 9-40853; 9-110998; 09-507514; 10-067924; 11-130856; 2000-109552; 2000-169683; 2000-226444; 2001-048966; 2001-81161; 2001-064377; 2001-064378; 97/47675; 98/38235; 98/56848; 00/24827 |
| Other References: |
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| Abstract: |
The present invention provides a catalyst for polyester production capable of producing a polyester with high catalytic activity, a process for producing a polyester using the catalyst and a polyester produced thereby. The catalyst comprises a solid titanium compound obtained by dehydro-drying a hydrolyzate obtained by hydrolysis of a titanium halide and which has a molar ratio (OH/Ti) of a hydroxyl group (OH) to titanium (Ti) exceeding 0.09 and less than 4. In the process, the polyester is obtained by polycondensing an aromatic dicarboxylic acid, or an ester-forming derivative thereof, and an aliphatic diol, or ester-forming derivative thereof, in the presence of the catalyst. The resulting polyester has excellent transparency and tint, a titanium content of 1 to 100 ppm, a magnesium content of 1 to 200 ppm and a magnesium to titanium weight ratio of not less than 0.01. |
| Claim: |
What is claimed is:
1. A catalyst for polyester production, comprising a solid titanium compound (I-a) which is obtained by dehydro-drying a hydrolyzate obtained by hydrolyzing a titanium halideand has a molar ratio (OH/Ti) of a hydroxyl group (OH) to titanium (Ti) exceeding 0.09 and less than 4.
2. A catalyst for polyester production, comprising a titanium-containing solid compound (I-b) which is obtained by dehydro-drying a hydrolyzate obtained by hydrolyzing a mixture of a titanium halide and a compound of at least one elementselected from elements other than titanium or a precursor of the compound and has a molar ratio (OH/Ti) of a hydroxyl group (OH) to titanium (Ti) exceeding 0.09 and less than 4.
3. The catalyst for polyester production as claimed in claim 2, wherein the compound of at least one element selected from elements other than titanium or the precursor of the compound is a compound of at least one element selected from thegroup consisting of beryllium, magnesium, calcium, strontium, barium, scandium, yttrium, lanthanium, zirconium, hafnium, vanadium, niobium, tantalum, chromium, molybdenum, tungsten, manganese, iron, ruthenium, cobalt, rhodium, nickel, palladium, cooper,zinc, boron, aluminum, gallium, silicon, germanium, tin, antimony and phosphorus or a precursor of the compound.
4. A catalyst for polyester production comprising: a polycondensation catalyst component comprising the solid titanium compound (I-a) of claim 1 or the titanium-containing solid compound (I-b) of claim 2, and (II) a co-catalyst componentcomprising a compound of at least one element selected from the group consisting of beryllium, magnesium, calcium, strontium, barium boron, aluminum, gallium, manganese, cobalt, zinc, germanium, antimony and phosphorus.
5. A catalyst for polyester production, comprising a solid titanium compound (I-f) obtained by a process comprising bringing a titanium halide into contact with water to hydrolyze the titanium halide and thereby obtain an acid solutioncontaining a hydrolyzate of the titanium halide, adjusting pH of the solution to 2 to 6 by the use of a base, and dehydro-drying the resulting precipitate.
6. A catalyst for polyester production, comprising a solid titanium compound (I-i) which is obtained by dehydro-drying titanium hydroxide and has a crystallinity, as calculated from an X-ray diffraction pattern having 2.theta. (diffractionangle) of 18.degree. to 35.degree., of not more than 50%.
7. A catalyst for polyester production, comprising: (I) a polycondensation catalyst component comprising the solid titanium compound (I-i) of claim 6, and (II) a co-catalyst component comprising a compound of at least one element selected fromthe group consisting of beryllium, magnesium, calcium, strontium, barium, boron, aluminum, gallium, manganese, cobalt, zinc, germanium, antimony and phosphorus.
8. A catalyst for polyester production, comprising a slurry obtained by heating a mixture of: (A-1) a hydrolyzate (I-j) obtained by hydrolyzing a titanium compound or a hydrolyzate (I-k) obtained by hydrolyzing a mixture of a titanium compoundand a compound of at least one element selected from elements other than titanium or a precursor of the compound, (B) a basic compound, and (C) an aliphatic diol.
9. The catalyst for polyester production as claimed in claim 8, wherein the basic compound (B) is at least one compound selected from tetraethylammonium hydroxide, tetraethylammonium hydroxide, aqueous ammonia, sodium hydroxide, potassiumhydroxide, N-ethylmorpholine and N-methylmorpholine.
10. The catalyst for polyester production as claimed in claim 8 or 9, wherein the aliphatic diol (C) is ethylene glycol.
11. A catalyst for polyester production, comprising: (A-2) a hydrolyzate (I-m) obtained by hydrolyzing a titanium halide or a hydrolyzate (I-n) obtained by hydrolyzing a mixture of a titanium halide and a compound of at least one elementselected from elements other than titanium or a precursor of the compound, and (D) a metallic phosphate containing at least one element selected from beryllium, magnesium, calcium, strontium, boron, aluminum, gallium, manganese, cobalt and zinc.
12. The catalyst for polyester production as claimed in claim 11, wherein the metallic phosphate (D) is magnesium hydrogenphosphate or trimagnesium diphosphate.
13. A catalyst for polyester production, comprising a slurry obtained by heating a mixture of: (A-2) a hydrolyzate (I-m) obtained by hydrolyzing a titanium halide or a hydrolyzate (I-n) obtained by hydrolyzing a mixture of a titanium halide anda component of at least one element selected from elements other than titanium or a precursor of the compound, (E) a metallic compound containing at least one element elected from beryllium, magnesium, calcium, strontium, boron, aluminum, gallium,manganese, cobalt and zinc, (F) at least one phosphors compound selected from phosphoric acid and phosphoric esters, and (G) an aliphatic diol.
14. The catalyst for polyester production as claimed in claim 13, wherein the metallic compound (E) is a magnesium compound, the phosphatic compound (F) is phosphoric acid or trimethyl phosphate, and the aliphatic diol (G) is ethylene glycol.
15. The catalyst for polyester production as claimed in claim 13 or 14, wherein the heating temperature of the mixture or the components (A-2), (E), (F) and (G) is in the range of 100 and 200.degree. C., and the heating time is in the range of3 minutes to 5 hours.
16. A process for producing a polyester comprising polycondensing an aromatic dicarboxylic acid or an ester-forming derivative thereof and an aliphatic diol or an ester-forming derivative thereof in the presence of the catalyst as claimed inany one of claims 1, 2, 5, 6, 8, 11, 13.
17. A process for producing a polyester, comprising an esterification step in which an aromatic dicarboxylic acid or an ester-forming derivative thereof and an aliphatic diol an ester-forming derivative thereof are esterified to form a lowcondensate and a polycondensation step in which the low condensate is polycondensed in the presence of a polycondensation catalyst to increase the molecular weight, wherein: the polycondensation catalyst used is a catalyst comprising: (I) apolycondensation catalyst component comprising a hydrolyzate (I-j) obtained by hydrolyzing a titanium compound or a hydrolyzate (I-k) obtained by hydrolyzing a mixture of a titanium compound and a compound of at least one element selected from elementsother than titanium or a precursor of the compound, and (II) a co-catalyst component comprising a compound of at least one element selected from the group consisting of beryllium, magnesium, calcium, strontium, barium, boron, aluminum, gallium,manganese, cobalt, zinc, germanium, antimony and phosphorus; and the polycondensation catalyst component (I) is added to the esterification reactor before the beginning of the esterification reaction or immediately after the beginning of theesterification reaction.
18. The process for producing a polyester as claimed in claim 17, wherein the co-catalyst component (II) is a magnesium compound.
19. A process for producing a polyester, comprising polycondensation an aromatic dicarboxylic acid or an ester-forming derivative thereof and an aliphatic diol or an ester-forming derivative thereof in the presence of a polycondensationcatalyst selected from the following catalysts (1) to (3) and a phosphoric ester to produce a polyester; (1) a polycondensation catalyst comprising a hydrolyzate (I-m) obtained by hydrolyzing a titanium halide, (2) a polycondensation catalyst comprisinga hydrolyzate (I-n) obtained by hydrolyzing a mixture of a titanium halide and a compound of at least one element selected from elements other than titanium or a precursor of the compound, and (3) a polycondensation catalyst comprising: the hydrolyzate(I-m) or (I-n), and a compound of at least one element selected from the group consisting of beryllium, magnesium, calcium, strontium, barium, boron, aluminum, gallium, manganese, cobalt, zinc, germanium and antimony, a phosphate or a phosphite.
20. The process for producing a polyester as claimed in claim 19, wherein the phosphoric ester is tributyl phosphate, trioctyl phosphate or triphenyl phosphate.
21. A process for producing a polyester, comprising polycondensing an aromatic dicarboxylic acid or an ester-forming derivative thereof and an aliphatic diol or an ester-forming derivative thereof in the presence of a polycondensation catalystselected from the following catalyst (1) to (3) and at least one compound selected from cyclic lactone compounds and hindered phenol compounds to produce a polyester; (1) a polycondensation catalyst comprising a hydrolyzate (I-m) obtained by hydrolyzinga titanium halide, (2) a polycondensation catalyst comprising a hydrolyzate (I-n) obtained by hydrolyzing a mixture of a titanium halide and a compound of at least one element selected from elements other than titanium or a precursor of the compound, and(3) a polycondensation catalyst comprising: the hydrolyzate (I-m) or (I-n), and a compound of at least one element selected from the group consisting of beryllium, magnesium, calcium, strontium,, barium, boron, aluminum, gallium, manganese, cobalt, zinc,germanium and antimony, a phosphate or a phosphite.
22. The process for producing a polyester as claimed in claim 21, wherein at least one phosphorus compound selected from phosphoric acid and phosphoric esters is further used in combination.
23. The process for producing a polyester as claimed in claim 21 or 22, wherein the at least one compound selected from cyclic lactone compounds and hindered phenol compounds is a mixture of5,7-t-butyl-3-(3,4-dimethylphenyl)-3H-benzofuran-2-one, tetrakis(methylene-3(3,5-di-t-butyl-4-hyroxyphenyl)propionate)methane and tris(2,4-di-t-butylphenyl)phosphite.
24. A process for producing a polyester, comprising an esterification step in which an aromatic dicarboxylic acid or an ester-forming derivative thereof and an aliphatic diol or an ester-forming derivative thereof are esterified to form a lowcondensate and a polycondensation step in which the low condensate is polycondensed in the presence of a polycondensation catalyst to increase the molecular weight, wherein: the polycondensation catalyst used is a catalyst comprising: (I) apolycondensation catalyst component comprising a hydrolyzate (I-m) obtained by hydrolyzing a titanium halide or a hydrolyzate (I-n) obtained by hydrolyzing a mixture of a titanium halide and a compound of at least one element selected from elements otherthan titanium or a precursor of the compound, and (II) a co-catalyst component comprising a compound of at least one element selected from the group consisting of beryllium, magnesium, calcium, strontium, barium, boron, aluminum, gallium, manganese,cobalt, zinc, germanium, antimony and phosphorus; and a tint adjusting agent is added in the esterification step or the polycondensation step.
25. The process for producing a polyester as claimed in claim 24, wherein the tint adjusting agent is at least one agent selected from Solvent Blue 104, Pigment Red 263, Solvent Red 135, Pigment Blue 29, Pigment Blue 15:1, Pigment Blue 15:3,Pigment Red 187 and Pigment Violet 19.
26. The process for producing a polyester as claimed in claim 24 or 25, wherein the co-catalyst component (II) is a magnesium compound.
27. A method for treating a polyester, comprising bringing a polyester, which is obtained by the use of titanium compound catalyst and in which the reaction has been completed, into contact with a phosphorus acid aqueous solution, a phosphoricester aqueous solution, a phosphorous ester aqueous solution or a hypophosphorous ester aqueous solution, each of said solution having a concentration of not less than 10 ppm in terms of phosphorus atom.
28. The method for treating a polyester as claimed in claim 27, wherein the polyester has an intrinsic viscosity of not less than 0.50 dl/g, a density of not less than 1.37 g/cm.sup.3 and an acetaldehyde content of not more than 5 ppm.
29. The method for treating a polyester as claimed in claim 27 or 28, wherein polyethylene terephthalate, which is obtained by the use of a titanium compound catalyst and in which the reaction has been completed, is treated.
30. A method for treating a polyester, comprising bringing a polyester, which is obtained by the use of a titanium compound catalyst and in which the reaction has been completed, into contact with an organic solvent.
31. The method for treating a polyester as claimed in claim 30, wherein the polyester has an intrinsic viscosity of not less than 0.50 dl/g, a density of not less than 1.37 g/cm.sup.3 and an acetaldehyde content of not more than 5 ppm.
32. The method for treating a polyester as claimed in claim 30 or 31, wherein the organic solvent is a solvent selected from alcohols, saturated hydrocarbons and ketones.
33. The method for treating a polyester as claimed in any one of claims 30 to 31, wherein the organic solvent is isopropanol or acetone.
34. The method of treating a polyester as claimed in any one of claims 30 to 31, wherein polyethylene terephthalate, which is obtained by the use of a titanium compound catalyst and in which the reaction has been completed, is treated.
35. A method for treating a polyester, comprising bringing polyester, which is obtained by the use of a titanium compound catalyst and in which the reaction has been completed, into contact with an organic solvent solution of phosphoric acid,an organic solvent solution of phosphoric ester, an organic solvent solution of phosphorous acid, an organic solvent solution of hypophosphorous acid, an organic solvent solution of a phosphorous ester or an organic solvent solution of a hypophosphorousester, each of said solutions having a concentration of not less than 10 ppm in terms of phosphorus atom.
36. The method for treating a polyester as claimed in claim 35, wherein the polyester has an intrinsic viscosity of not less than 0.50 dl/g, a density of not less than 1.37 g/cm.sup.3 and an acetaldehyde content of not more than 5 ppm.
37. The method for treating a polyester as claimed in claim 35 or 36, wherein the phosphoric ester is tributyl phosphate, triphenyl phosphate or trimethyl phosphate.
38. The method for treating a polyester as claimed in claim 35, wherein the organic solvent is selected from alcohols, saturated hydrocarbons and ketones.
39. The method for treating a polyester as claimed in claim 35, wherein the organic solvent is isopropanol or acetone.
40. The method for treating a polyester as claimed in claim 35, wherein polyethylene terephthalate, which is obtained by the use of a titanium compound catalyst and in which the reaction has been completed, is treated.
41. A polyester (P-1) obtained by polycondensing an aromatic dicarboxylic acid or an ester-forming derivative thereof and an aliphatic diol or an ester-forming derivative thereof in the presence of a catalyst for polyester productioncomprising: a polycondensation catalyst component comprising a solid titanium compound (I-c) obtained by dehydro-drying a hydrolyzate obtained by hydrolyzing a titanium halide, and (II) a co-catalyst comprising a compound of at least one element selectedfrom the group consisting of beryllium, magnesium, calcium, strontium, barium, boron, aluminum, gallium, manganese, cobalt, zinc, germanium, antimony and phosphorus, wherein the titanium content is in the range 1 to 100 ppm, the magnesium content is inthe range of 1 to 200 ppm, and the weight ratio (Mg/Ti) of magnesium to titanium is not less than 0.01.
42. The polyester (P-1) as claimed in claim 41, which is polyethylene terephthalate.
43. A polyester (P-2) having the following properties: a titanium atom is contained in an amount of 0.1 to 200 ppm, a metal atom M selected from beryllium, magnesium, calcium, strontium, barium, boron, aluminum, gallium, manganese, cobalt, zincand antimony is contained in an amount of 0.1 to 500 ppm, the molar ratio (titanium atom/metal atom M) of the titanium atom to the metal atom M is in the range of 1/50 to 50/1, and a tint adjusting agent is contained in an amount of 0.01 to 100 ppm.
44. A polyester (P-3) having the following properties: the intrinsic viscosity is not less than 0.50 dl/g, a titanium atom is contained in an amount of 0.1 to 200 ppm, a metal atom M selected from beryllium, magnesium, calcium, strontium,barium, boron, aluminum, gallium, manganese, cobalt, zinc and antimony is contained in an amount of 0.1 to 500 ppm, the molar ratio (titanium atom/metal atom M) of the titanium atom to the metal atom M is in the range of 0.05 to 50, and the content ofacetaldehyde is not more than 4 ppm, and when this acetaldehyde content is taken as W.sub.0 ppm and a content of acetaldehyde in a stepped square plate molded product obtained by heating said polyester to a temperature of 275.degree. C. to melt it andmolding the molten polyester is taken as W.sub.1 ppm, the value of W.sub.1-W.sub.0 is not more than 10 ppm.
45. The polyester (P-3) as claimed in claim 44, wherein the titanium atom is derived from a polycondensation catalyst obtained by hydrolysis of a titanium halide.
46. The polyester (P-3) as claimed in claim 44 or 45, which is polyethylene terephthalate.
47. A polyester (P-4) having the following properties: the intrinsic viscosity is not less than 0.50 dl/g, a titanium atom is contained in an amount of 0.1 to 200 ppm, a metal atom M selected from beryllium, magnesium, calcium, strontium,barium, boron, aluminum, gallium, manganese, cobalt, zinc and antimony is contained in an amount of 0.1 to 500 ppm, the molar ratio (titanium atom/metal atom M) of the titanium atom to the metal atom M is in the range of 0.05 to 50, and the content of acyclic trimer is not more than 0.5% by weight, and when this cyclic trimer content is taken as x % by weight and .[.a content of a.]. .Iadd.an increase in .Iaddend.cyclic trimer in a stepped square plate molded product obtained by heating said polyesterto a temperature of 290.degree. C. to melt it and molding the molten polyester is taken as y % by weight, x and y satisfy the following relation .[.y.ltoreq.-0.2x-0.2.]. .Iadd.y.ltoreq.-0.2x+0.2.Iaddend..
48. The polyester (P-4) as claimed in claim 47, wherein the titanium atom is derived from a polycondensation catalyst obtained by hydrolysis of at titanium halide.
49. The polyester (P-4) as claimed in claim 47 or 48, which is polyethylene terephthalate.
50. A molded product obtained from the polyester (P-1) as claimed in any one of the claims 41 or 42.
51. The molded product as claimed in claim 50, which is a blow molded article.
52. The molded product as claimed in claim 50, which is a film or a sheet.
53. The molded product as claimed in claim 50, which is a fiber.
54. A blow molded article obtained from the polyester (P-4) as claimed in any of claims 47 or 48 and having a cyclic trimer content of not more than 0.6% by weight.
55. A perform for a blow molded article which is obtained from a polyester (P-5) having the following properties: when the ratio (L/T) of a flow length (L) to a flow thickness (T) in the injection molding of said polyester at 290.degree. C. istaken as Y and the intrinsic viscosity of a molded product obtained by the injection molding is taken as X(dl/g), X and Y satisfy the following relation Y.gtoreq.647-500X.
56. A blow molded article obtained from the perform of claim 55. |
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