U.S. patent application number 11/449645 was filed with the patent office on 2006-10-12 for polyester resin and process for its production.
This patent application is currently assigned to MITSUBISHI CHEMICAL CORPORATION. Invention is credited to Yoshihiro Fujimori, Kenichi Matsui, Masahiro Nukui, Yutaka Yatsugi.
Application Number | 20060229429 11/449645 |
Document ID | / |
Family ID | 18893515 |
Filed Date | 2006-10-12 |
United States Patent
Application |
20060229429 |
Kind Code |
A1 |
Fujimori; Yoshihiro ; et
al. |
October 12, 2006 |
Polyester resin and process for its production
Abstract
A polyester resin characterized in that the content of the
copolymerized components other than the terephthalic acid component
and the ethylene glycol component, is not more than 4 mol % based
on the total dicarboxylic acid component, and when polyester resin
is formed into a molded product, the molded product has a specific
absorbance.
Inventors: |
Fujimori; Yoshihiro; (Mie,
JP) ; Nukui; Masahiro; (Mie, JP) ; Yatsugi;
Yutaka; (Mie, JP) ; Matsui; Kenichi; (Mie,
JP) |
Correspondence
Address: |
C. IRVIN MCCLELLAND;OBLON, SPIVAK, MCCLELLAND, MAIER & NEUSTADT, P.C.
1940 DUKE STREET
ALEXANDRIA
VA
22314
US
|
Assignee: |
MITSUBISHI CHEMICAL
CORPORATION
Tokyo
JP
|
Family ID: |
18893515 |
Appl. No.: |
11/449645 |
Filed: |
June 9, 2006 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
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11294368 |
Dec 6, 2005 |
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11449645 |
Jun 9, 2006 |
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10650790 |
Aug 29, 2003 |
6998463 |
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11294368 |
Dec 6, 2005 |
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10263716 |
Oct 4, 2002 |
6667383 |
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10650790 |
Aug 29, 2003 |
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PCT/JP02/00981 |
Feb 6, 2002 |
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10263716 |
Oct 4, 2002 |
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Current U.S.
Class: |
528/279 |
Current CPC
Class: |
C08G 63/83 20130101;
C08G 63/87 20130101; C08G 63/85 20130101; C08G 63/82 20130101; C08G
63/183 20130101; C08G 63/826 20130101 |
Class at
Publication: |
528/279 |
International
Class: |
C08G 63/00 20060101
C08G063/00 |
Foreign Application Data
Date |
Code |
Application Number |
Feb 6, 2001 |
JP |
2001-29135 |
Claims
1.-15. (canceled)
16. A polyester resin produced by polycondensing a dicarboxylic
acid component containing terephthalic acid or its ester-forming
derivative as the main component, and a diol component containing
ethylene glycol as the main component in the presence of (1) a
compound of at least one member selected from the group consisting
of titanium group elements in Group 4A of the periodic table, via
an esterification reaction or an ester exchange reaction, wherein
said polyester resin is obtained by melt polycondensation wherein
the intrinsic viscosity ([.eta..sub.1]) ranges from 0.35 to 0.75
dl/g as a value measured at 30.degree. C. in a solution in a mixed
solvent of phenol/tetrachloroethane (weight ratio: 1/1) and wherein
the melt polycondensation velocity (V.sub.1) as a value obtained by
dividing the intrinsic viscosity ([.eta..sub.1]) of the resulting
polyester resin by the reaction time, is at least 0.15 dl/g/hr.
17. The polyester resin according to claim 16, wherein the
temperature-rising crystallization temperature (Tc) of the resin in
the molded product after the injection molding at 280.degree. C.,
is from 150 to 180.degree. C.
18. The polyester resin according to claim 16, wherein the resin
before the injection molding is one having an intrinsic viscosity
([.eta.]) of from 0.70 to 0.90 dl/g and a color coordinate value b
of the Hunter's color difference formula of not more than 4.
19. The polyester resin according to claim 16, wherein the content
of the compound (1) is from 0.002 to 1 mol as the total amount (T)
of atoms of the compound (1) per 1 ton of the polyester resin.
20. The polyester resin according to claim 19, which is one
polycondensed in the coexistence of (2) a compound of at least one
element selected from the group consisting of metal elements of
Group Ia of the periodic table, elements of Group IIa of the
periodic table, manganese, iron and cobalt, and (3) a phosphorus
compound, wherein the content of the compound (2) is from 0.04 to 5
mols as the total amount (M) of atoms of the compound (2) per 1 ton
of the polyester resin, and the content of the compound (3) is from
0.02 to 4 mols as the total amount (P) of atoms of the compound (3)
per 1 ton of the polyester resin.
21. The polyester resin according to claim 20, wherein the contents
of the respective compounds (1), (2) and (3) are from 0.02 to 0.2
mol as the total amount (T) of atoms of the compound (1), from 0.04
to 0.6 mol as the total amount (M) of atoms of the compound (2) and
from 0.02 to 0.4 mol as the total amount (P) of atoms of the
compound (3), per 1 ton of the polyester resin, the acetaldehyde
content (AA.sub.1) is not more than 5.0 ppm, the acetaldehyde
content (AA.sub.2) of the resin in a molded product after
injection-molded at 280.degree. C. is not more than 20 ppm, and the
haze of a molded product with a thickness of 5 mm after the
injection molding at 280.degree. C. is not more than 10%.
22. The polyester resin according to claim 16, wherein the compound
(1) is a titanium compound, the compound (2) is a magnesium
compound, and the compound (3) is a phosphoric acid ester.
23. The polyester resin according to claim 16, wherein, as a
dicarboxylic acid component, from 0.1 to 3 mol % of isophthalic
acid or its ester-forming derivative based on the total
dicarboxylic acid component, and as a diol component, from 1 to 3
mol % of diethylene glycol based on the total diol component, are
copolymerized, respectively.
24. A process for producing the polyester resin according to claim
16, which comprises polycondensing a dicarboxylic acid component
containing terephthalic acid or its ester-forming derivative as the
main component, and a diol component containing ethylene glycol as
the main component in the presence of (1) a compound of at least
one member selected from the group consisting of titanium group
elements in Group 4A of the periodic table, (2) a compound of at
least one element selected from the group consisting of metal
elements of Group Ia of the periodic table, elements of Group IIa
of the periodic table, manganese, iron and cobalt, and (3) a
phosphorus compound, via an esterification reaction or an ester
exchange reaction, characterized in that the amounts of the
respective compounds (1), (2) and (3) are such amounts that their
contents will be from 0.02 to 0.2 mol as the total amount (T) of
atoms of the compound (1), from 0.04 to 0.6 mol as the total amount
(M) of atoms of the compound (2) and from 0.02 to 0.4 mol as the
total amount (P) of atoms of the compound (3), per 1 ton of the
polyester resin.
25. The process for producing a polyester resin according to claim
24, wherein the ratio (P/T) of the total amount (P) of atoms of the
compound (3) to the total amount (T) of atoms of the compound (1),
is from 0.1 to 10.
26. The process for producing a polyester resin according to claim
24, wherein the ratio (M/T) of the total amount (M) of atoms of the
compound (2) to the total amount (T) of atoms of the compound (1),
is from 0.1 to 10.
27. The process for producing a polyester resin according to claim
24, wherein the order for addition of the respective compounds (1),
(2) and (3) to the reaction system is (3), then (2) and then
(1).
28. The process for producing a polyester resin according to claim
24, wherein the compound (1) is a titanium compound, the compound
(2) is a magnesium compound, and the compound (3) is a phosphoric
acid ester.
29. The process for producing a polyester resin according to claim
28, wherein the titanium compound is added to the reaction system
in the form of an ethylene glycol solution having a titanium atom
concentration of from 0.01 to 0.3 wt % and a water concentration of
from 0.1 to 1 wt %.
30. The process for producing a polyester resin according to claim
24, wherein from 0.1 to 3 mol % of isophthalic acid or its
ester-forming derivative is used based on the total dicarboxylic
acid component.
31. A process for producing the polyester resin of claim 16, which
comprises polycondensing a dicarboxylic acid component containing
terephthalic acid or its ester-forming derivative as the main
component and a diol component containing ethylene glycol as the
main component in the presence of (1) a compound of at least one
member selected from the group consisting of titanium group
elements in Group 4A of the Periodic Table, via an esterification
reaction or an ester exchange reaction, wherein the above compound
(1) is added to an esterification reaction tank for a final stage
in a multi-stage reaction apparatus or to an esterification
reaction or ester exchange reaction product in a stage for
transportation to a melt polycondensation step.
32. The process for producing a polyester resin according to claim
31 which comprises polycondensing terephthalic acid and ethylene
glycol in the presence of (1) a compond of at least one member
selected from the group consisting of titanium group elements in
Group 4A of the Periodic Table, via an esterification reaction,
wherein the above compound (1) is added to an esterification
reaction tank for a final stage in a multi-stage reaction apparatus
or to an esterification reaction product in a stage for
transportation to a melt polycondensation step.
33. The process for producing a polyester resin according to claim
31, wherein the compound (1) is added at such a stage as an
esterification rate of an esterification reaction or ester exchange
reaction product becomes at least 90%.
34. The process for producing a polyester resin according to claim
31, wherein the compound (1) is added to an esterification reaction
product in a stage for transportation to a melt polycondensation
step.
35. The process for producing a polyester resin according to claim
31, wherein the polycondensation is carried out in the presence of
(2) a compound of at least one member selected from the group
consisting of metal elements of Group 1A of the Periodic Table,
elements of Group 2A of the Periodic Table, manganese, iron and
cobalt and (3) a phosphorus compound.
36. The process for producing a polyester resin according to claim
35, wherein a compound of at least one element selected from the
group consisting of metal elements of Group 1A of the Periodic
Table, elements of Group 2A of the Periodic Table, manganese, iron
and cobalt is added to an esterification reaction tank for a final
stage in a multistage reaction apparatus.
37. The process for producing a polyester resin according to claim
31, wherein the compound (1) is a titanium compound.
38. A polyester resin produced by polycondensing a dicarboxylic
acid component containing terephthalic acid or its ester-forming
derivative as the main component, and a diol component containing
ethylene glycol as the main component in the presence of (1) a
compound of at least one member selected from the group consisting
of titanium group elements in Group 4A of the periodic table, via
an esterification reaction or an ester exchange reaction, wherein
said polyester resin is obtained by solid phase polycondensation is
wherein the intrinsic viscosity ([.eta..sub.2]) ranges from 0.70 to
0.90 dl/g as a value measured at 30.degree. C. in a solution in a
mixed solvent of phenol/tetrachloroethane (weight ratio: 1/1) and
wherein the solid phase polycondensation velocity (V.sub.2) as a
value obtained by dividing the difference
([.eta..sub.2]-[.eta..sub.1]) between the intrinsic viscosity
([.eta..sub.2]) of the obtainable solid phase polycondensation
resin and the intrinsic viscosity ([.eta..sub.1]) of the melt
polycondensation resin, by the reaction time, ranges from 0.008 to
0.015 dl/g/hr.
39. The polyester resin according to claim 38, wherein the
temperature-rising crystallization temperature (Tc) of the resin in
the molded product after the injection molding at 280.degree. C.,
is from 150 to 180.degree. C.
40. The polyester resin according to claim 38, wherein the resin
before the injection molding is one having an intrinsic viscosity
([.eta.]) of from 0.70 to 0.90 dl/g and a color coordinate value b
of the Hunter's color difference formula of not more than 4.
41. The polyester resin according to claim 38, wherein the content
of the compound (1) is from 0.002 to 1 mol as the total amount (T)
of atoms of the compound (1) per 1 ton of the polyester resin.
42. The polyester resin according to claim 41, which is one
polycondensed in the coexistence of (2) a compound of at least one
element selected from the group consisting of metal elements of
Group Ia of the periodic table, elements of Group IIa of the
periodic table, manganese, iron and cobalt, and (3) a phosphorus
compound, wherein the content of the compound (2) is from 0.04 to 5
mols as the total amount (M) of atoms of the compound (2) per 1 ton
of the polyester resin, and the content of the compound (3) is from
0.02 to 4 mols as the total amount (P) of atoms of the compound (3)
per 1 ton of the polyester resin.
43. The polyester resin according to claim 42, wherein the contents
of the respective compounds (1), (2) and (3) are from 0.02 to 0.2
mol as the total amount (T) of atoms of the compound (1), from 0.04
to 0.6 mol as the total amount (M) of atoms of the compound (2) and
from 0.02 to 0.4 mol as the total amount (P) of atoms of the
compound (3), per 1 ton of the polyester resin, the acetaldehyde
content (AA.sub.1) is not more than 5.0 ppm, the acetaldehyde
content (AA.sub.2) of the resin in a molded product after
injection-molded at 280.degree. C. is not more than 20 ppm, and the
haze of a molded product with a thickness of 5 mm after the
injection molding at 280.degree. C. is not more than 10%.
44. The polyester resin according to claim 38, wherein the compound
(1) is a titanium compound, the compound (2) is a magnesium
compound, and the compound (3) is a phosphoric acid ester.
45. The polyester resin according to claim 38, wherein, as a
dicarboxylic acid component, from 0.1 to 3 mol % of isophthalic
acid or its ester-forming derivative based on the total
dicarboxylic acid component, and as a diol component, from 1 to 3
mol % of diethylene glycol based on the total diol component, are
copolymerized, respectively.
46. A process for producing the polyester resin according to claim
38, which comprises polycondensing a dicarboxylic acid component
containing terephthalic acid or its ester-forming derivative as the
main component, and a diol component containing ethylene glycol as
the main component in the presence of (1) a compound of at least
one member selected from the group consisting of titanium group
elements in Group 4A of the periodic table, (2) a compound of at
least one element selected from the group consisting of metal
elements of Group Ia of the periodic table, elements of Group IIa
of the periodic table, manganese, iron and cobalt, and (3) a
phosphorus compound, via an esterification reaction or an ester
exchange reaction, characterized in that the amounts of the
respective compounds (1), (2) and (3) are such amounts that their
contents will be from 0.02 to 0.2 mol as the total amount (T) of
atoms of the compound (1), from 0.04 to 0.6 mol as the total amount
(M) of atoms of the compound (2) and from 0.02 to 0.4 mol as the
total amount (P) of atoms of the compound (3), per 1 ton of the
polyester resin.
47. The process for producing a polyester resin according to claim
46, wherein the ratio (P/T) of the total amount (P) of atoms of the
compound (3) to the total amount (T) of atoms of the compound (1),
is from 0.1 to 10.
48. The process for producing a polyester resin according to claim
46, wherein the ratio (M/T) of the total amount (M) of atoms of the
compound (2) to the total amount (T) of atoms of the compound (1),
is from 0.1 to 10.
49. The process for producing a polyester resin according to claim
46, wherein the order for addition of the respective compounds (1),
(2) and (3) to the reaction system is (3), then (2) and then
(1).
50. The process for producing a polyester resin according to claim
46, wherein the compound (1) is a titanium compound, the compound
(2) is a magnesium compound, and the compound (3) is a phosphoric
acid ester.
51. The process for producing a polyester resin according to claim
50, wherein the titanium compound is added to the reaction system
in the form of an ethylene glycol solution having a titanium atom
concentration of from 0.01 to 0.3 wt % and a water concentration of
from 0.1 to 1 wt %.
52. The process for producing a polyester resin according to claim
46, wherein from 0.1 to 3 mol % of isophthalic acid or its
ester-forming derivative is used based on the total dicarboxylic
acid component.
53. A process for producing the polyester resin of claim 38, which
comprises polycondensing a dicarboxylic acid component containing
terephthalic acid or its ester-forming derivative as the main
component and a diol component containing ethylene glycol as the
main component in the presence of (1) a compound of at least one
member selected from the group consisting of titanium group
elements in Group 4A of the Periodic Table, via an esterification
reaction or an ester exchange reaction, wherein the above compound
(1) is added to an esterification reaction tank for a final stage
in a multi-stage reaction apparatus or to an esterification
reaction or ester exchange reaction product in a stage for
transportation to a melt polycondensation step.
54. The process for producing a polyester resin according to claim
53 which comprises polycondensing terephthalic acid and ethylene
glycol in the presence of (1) a compond of at least one member
selected from the group consisting of titanium group elements in
Group 4A of the Periodic Table, via an esterification reaction,
wherein the above compound (1) is added to an esterification
reaction tank for a final stage in a multi-stage reaction apparatus
or to an esterification reaction product in a stage for
transportation to a melt polycondensation step.
55. The process for producing a polyester resin according to claim
53, wherein the compound (1) is added at such a stage as an
esterification rate of an esterification reaction or ester exchange
reaction product becomes at least 90%.
56. The process for producing a polyester resin according to claim
53, wherein the compound (1) is added to an esterification reaction
product in a stage for transportation to a melt polycondensation
step.
57. The process for producing a polyester resin according to claim
53, wherein the polycondensation is carried out in the presence of
(2) a compound of at least one member selected from the group
consisting of metal elements of Group 1A of the Periodic Table,
elements of Group 2A of the Periodic Table, manganese, iron and
cobalt and (3) a phosphorus compound.
58. The process for producing a polyester resin according to claim
57, wherein a compound of at least one element selected from the
group consisting of metal elements of Group 1A of the Periodic
Table, elements of Group 2A of the Periodic Table, manganese, iron
and cobalt is added to an esterification reaction tank for a final
stage in a multistage reaction apparatus.
59. The process for producing a polyester resin according to claim
53, wherein the compound (1) is a titanium compound.
60. A polyester resin produced by polycondensing a dicarboxylic
acid component containing terephthalic acid or its ester-forming
derivative as the main component, and a diol component containing
ethylene glycol as the main component in the presence of (1) a
compound of at least one member selected from the group consisting
of titanium group elements in Group 4A of the periodic table, via
an esterification reaction or an ester exchange reaction, wherein
said polyester resin is produced via melt polycondensation and
solid phase polycondensation, and wherein wherein the intrinsic
viscosity ([.eta..sub.1]) of the melt polycondensation resin ranges
from 0.35 to 0.75 dl/g as a value measured at 30.degree. C. in a
solution in a mixed solvent of phenol/tetrachloroethane (weight
ratio: 1/1) and wherein the melt polycondensation velocity
(V.sub.1) as a value obtained by dividing the intrinsic viscosity
([.eta..sub.1]) of the resulting polyester resin by the reaction
time, is at least 0.15 dl/g/hr, and wherein the intrinsic viscosity
([.eta..sub.2]) of the solid phase polycondensation ranges from
0.70 to 0.90 dl/g as a value measured at 30.degree. C. in a
solution in a mixed solvent of phenol/tetrachloroethane (weight
ratio: 1/1) and wherein the solid phase polycondensation velocity
(V.sub.2) as a value obtained by dividing the difference
([.eta..sub.2]-[.eta..sub.1]) between the intrinsic viscosity
([.eta..sub.2]) of the obtainable solid phase polycondensation
resin and the intrinsic viscosity ([.eta..sub.1]) of the melt
polycondensation resin, by the reaction time, ranges from 0.008 to
0.015 dl/g/hr.
61. The polyester resin according to claim 60, wherein the
temperature-rising crystallization temperature (Tc) of the resin in
the molded product after the injection molding at 280.degree. C.,
is from 150 to 180.degree. C.
62. The polyester resin according to claim 60, wherein the resin
before the injection molding is one having an intrinsic viscosity
([.eta.]) of from 0.70 to 0.90 dl/g and a color coordinate value b
of the Hunter's color difference formula of not more than 4.
63. The polyester resin according to claim 60, wherein the content
of the compound (1) is from 0.002 to 1 mol as the total amount (T)
of atoms of the compound (1) per 1 ton of the polyester resin.
64. The polyester resin according to claim 63, which is one
polycondensed in the coexistence of (2) a compound of at least one
element selected from the group consisting of metal elements of
Group Ia of the periodic table, elements of Group IIa of the
periodic table, manganese, iron and cobalt, and (3) a phosphorus
compound, wherein the content of the compound (2) is from 0.04 to 5
mols as the total amount (M) of atoms of the compound (2) per 1 ton
of the polyester resin, and the content of the compound (3) is from
0.02 to 4 mols as the total amount (P) of atoms of the compound (3)
per 1 ton of the polyester resin.
65. The polyester resin according to claim 64, wherein the contents
of the respective compounds (1), (2) and (3) are from 0.02 to 0.2
mol as the total amount (T) of atoms of the compound (1), from 0.04
to 0.6 mol as the total amount (M) of atoms of the compound (2) and
from 0.02 to 0.4 mol as the total amount (P) of atoms of the
compound (3), per 1 ton of the polyester resin, the acetaldehyde
content (AA.sub.1) is not more than 5.0 ppm, the acetaldehyde
content (AA.sub.2) of the resin in a molded product after
injection-molded at 280.degree. C. is not more than 20 ppm, and the
haze of a molded product with a thickness of 5 mm after the
injection molding at 280.degree. C. is not more than 10%.
66. The polyester resin according to claim 60, wherein the compound
(1) is a titanium compound, the compound (2) is a magnesium
compound, and the compound (3) is a phosphoric acid ester.
67. The polyester resin according to claim 60, wherein, as a
dicarboxylic acid component, from 0.1 to 3 mol % of isophthalic
acid or its ester-forming derivative based on the total
dicarboxylic acid component, and as a diol component, from 1 to 3
mol % of diethylene glycol based on the total diol component, are
copolymerized, respectively.
68. A process for producing the polyester resin according to claim
60, which comprises polycondensing a dicarboxylic acid component
containing terephthalic acid or its ester-forming derivative as the
main component, and a diol component containing ethylene glycol as
the main component in the presence of (1) a compound of at least
one member selected from the group consisting of titanium group
elements in Group 4A of the periodic table, (2) a compound of at
least one element selected from the group consisting of metal
elements of Group Ia of the periodic table, elements of Group IIa
of the periodic table, manganese, iron and cobalt, and (3) a
phosphorus compound, via an esterification reaction or an ester
exchange reaction, characterized in that the amounts of the
respective compounds (1), (2) and (3) are such amounts that their
contents will be from 0.02 to 0.2 mol as the total amount (T) of
atoms of the compound (1), from 0.04 to 0.6 mol as the total amount
(M) of atoms of the compound (2) and from 0.02 to 0.4 mol as the
total amount (P) of atoms of the compound (3), per 1 ton of the
polyester resin.
69. The process for producing a polyester resin according to claim
68, wherein the ratio (P/T) of the total amount (P) of atoms of the
compound (3) to the total amount (T) of atoms of the compound (1),
is from 0.1 to 10.
70. The process for producing a polyester resin according to claim
68, wherein the ratio (M/T) of the total amount (M) of atoms of the
compound (2) to the total amount (T) of atoms of the compound (1),
is from 0.1 to 10.
71. The process for producing a polyester resin according to claim
68, wherein the order for addition of the respective compounds (1),
(2) and (3) to the reaction system is (3), then (2) and then
(1).
72. The process for producing a polyester resin according to claim
68, wherein the compound (1) is a titanium compound, the compound
(2) is a magnesium compound, and the compound (3) is a phosphoric
acid ester.
73. The process for producing a polyester resin according to claim
72, wherein the titanium compound is added to the reaction system
in the form of an ethylene glycol solution having a titanium atom
concentration of from 0.01 to 0.3 wt % and a water concentration of
from 0.1 to 1 wt %.
74. The process for producing a polyester resin according to claim
68, wherein from 0.1 to 3 mol % of isophthalic acid or its
ester-forming derivative is used based on the total dicarboxylic
acid component.
75. A process for producing the polyester resin of claim 60, which
comprises polycondensing a dicarboxylic acid component containing
terephthalic acid or its ester-forming derivative as the main
component and a diol component containing ethylene glycol as the
main component in the presence of (1) a compound of at least one
member selected from the group consisting of titanium group
elements in Group 4A of the Periodic Table, via an esterification
reaction or an ester exchange reaction, wherein the above compound
(1) is added to an esterification reaction tank for a final stage
in a multi-stage reaction apparatus or to an esterification
reaction or ester exchange reaction product in a stage for
transportation to a melt polycondensation step.
76. The process for producing a polyester resin according to claim
75, which comprises polycondensing terephthalic acid and ethylene
glycol in the presence of (1) a compond of at least one member
selected from the group consisting of titanium group elements in
Group 4A of the Periodic Table, via an esterification reaction,
wherein the above compound (1) is added to an esterification
reaction tank for a final stage in a multi-stage reaction apparatus
or to an esterification reaction product in a stage for
transportation to a melt polycondensation step.
77. The process for producing a polyester resin according to claim
75, wherein the compound (1) is added at such a stage as an
esterification rate of an esterification reaction or ester exchange
reaction product becomes at least 90%.
78. The process for producing a polyester resin according to claim
75, wherein the compound (1) is added to an esterification reaction
product in a stage for transportation to a melt polycondensation
step.
79. The process for producing a polyester resin according to claim
75, wherein the polycondensation is carried out in the presence of
(2) a compound of at least one member selected from the group
consisting of metal elements of Group 1A of the Periodic Table,
elements of Group 2A of the Periodic Table, manganese, iron and
cobalt and (3) a phosphorus compound.
80. The process for producing a polyester resin according to claim
79, wherein a compound of at least one element selected from the
group consisting of metal elements of Group 1A of the Periodic
Table, elements of Group 2A of the Periodic Table, manganese, iron
and cobalt is added to an esterification reaction tank for a final
stage in a multistage reaction apparatus.
81. The process for producing a polyester resin according to claim
75, wherein the compound (1) is a titanium compound.
82. The polyester resin according to claim 60, wherein the ratio
(V.sub.2/V.sub.1) of this solid phase polycondensation velocity to
the melt polycondensation velocity is within a range of from 0.04
to 0.07.
Description
TECHNICAL FIELD
[0001] The present application claims a benefit of Japanese Patent
Application No. 2001-29135, and the content of this application
will be referred to as a reference in the present
specification.
[0002] The present invention relates to a polyester resin, whereby
a molded product excellent in a gas barrier property and also
excellent in an ultraviolet shielding property, a color tone, etc.,
and which is particularly suitable for molding a bottle for e.g. a
beverage required to have an aroma retention property, and further,
to a polyester resin, whereby the acetaldehyde content in a molded
product is reduced to eliminate an influence over the taste, aroma,
etc. of the content, and a process for its production, whereby the
polycondensability is improved.
BACKGROUND ART
[0003] Heretofore, a polyester resin such as a polyethylene
terephthalate resin has been widely used for packaging containers
for various beverages, etc., since it is excellent in mechanical
strength, chemical stability, gas barrier property, aroma-retention
property, hygienics, etc., and is relatively inexpensive and light
in weight. Especially, as a container for a beverage which requires
heat sterilization filling, for e.g. a fruit juice beverage, a
bottle having a high gas barrier property, etc. imparted by an
application of stretch heat setting, has shown a rapid expansion.
Such a bottle is produced, for example, by injection molding a
bottomed tubular preform, reheating the preform to soften it,
followed by stretch blow molding. At that time, the blow mold is
heated to apply heat setting to the bottle, whereby crystals of
molecular chains aligned by stretching are fixed to provide the
high gas barrier property, etc.
[0004] However, with respect to the polyethylene terephthalate
resin to be used in such a field of beverage containers, in the
case of a polyethylene terephthalate resin produced by using an
antimony compound as a polycondensation catalyst, which is most
commonly used for bottles for wide range of purpose,
copolymerizable components such as isophthalic acid, diethylene
glycol, etc. other than the terephthalic acid component and the
ethylene glycol component, are copolymerized in an amount of from
about 3 to 10 mol % based on the total dicarboxylic acid component
in order to provide transparency, whereby the intended gas barrier
property may not be obtained, whereby the aroma-retention property
as a bottle tends to decrease, and the aroma of the content is
likely to decrease, or the ultraviolet shielding property tends to
be poor, whereby the flavor component or the color tone of the
content is likely to deteriorate, and further, another problem is
also worried such that antimony remaining in the resin will elute
from the container at a high temperature and will transfer to the
contained beverage although slightly. On the other hand, with a
polyethylene terephthalate resin prepared by using a germanium
compound as a polycondensation catalyst, which is commonly used for
heat resistant bottles, copolymerizable components other than the
terephthalic acid component and the ethylene glycol component, may
be copolymerized in a relatively small amount at a level of more
than 2 to 5 mol % based on the total dicarboxylic acid component,
but the above-mentioned problem relating to a decrease of the
aroma-retention property cannot still be solved, and the
ultraviolet shielding property is also inferior, and further, the
germanium compound is expensive, whereby an economical disadvantage
cannot be avoided. Accordingly, it is strongly desired to have a
substitute polycondensation catalyst developed.
[0005] Further, many polyethylene terephthalate resins have been
proposed which are prepared by using titanium compounds as
polycondensation catalysts, but they have had problems such that
they lack in thermal stability, so that the obtainable resins tend
to have a yellowish color tone, or the change in the color tone
after being heated is substantial, and further have problems such
that acetaldehyde, a cyclic trimer, etc. are formed in a large
amount as by-products during the polycondensation and the melt
molding, and when used as bottles, they tend to deteriorate the
tastes, aromas, etc. of the contained beverages. Whereas, e.g.
JP-A-8-73581 discloses a process for producing a polyethylene
terephthalate resin which is colorless and excellent in
transparency, by using a titanium compound, a cobalt compound, and
a limited amount of complex-forming agent, such as phosphoric acid,
phosphorous acid and/or phosphonic acid or its derivative. However,
according to the study conducted by the present inventors, it has
been found that the polyethylene terephthalate resin obtainable by
this process is not one which is able to solve the above-mentioned
problem such as a decrease in the aroma-retention property and the
problem such as deterioration of the taste, the aroma, etc. of the
content.
[0006] Further, EP-A-1013692 discloses that production of
acetaldehyde as a by-product during the polycondensation and the
melt molding can be suppressed by using titanium and metal
compounds, as polycondensation catalysts, so that specific amounts
of titanium atoms and metal atoms such as magnesium, would be in a
specific ratio. Further, in JP-A-2000-339919 filed by the present
applicants, it is disclosed that in the polycondensation in the
presence of (1) a titanium compound, (2) a compound of at least one
element selected from the group consisting of metal elements of
Group 1A of the periodic table, elements of Group 2A of the
periodic table and manganese, and (3) a phosphorus compound, the
order of addition of the respective compounds (1), (2) and (3) is
set to be (3), then (2) and then (1), whereby by-products such as
acetaldehyde, a cyclic trimer, etc., can be reduced. However,
according to the study by the present inventors, it has been found
that these methods are certainly effective to reduce by-products,
but with the disclosed methods, there is still a room for
improvement with respect to the gas barrier property, the
ultraviolet shielding property or the polycondensability.
[0007] The present invention has been made in view of the
above-described prior art, and it is an object of the present
invention to provide a polyester resin, whereby a molded product
excellent in the gas barrier property and also excellent in the
ultraviolet shielding property, the color tone, etc., and which is
particularly suitable for molding a bottle for e.g. a beverage
required to have an aroma-retention property, and further, a
polyester resin, whereby the acetaldehyde content as a molded
product is reduced to eliminate an influence over the taste, the
aroma, etc. of the content, and a process for its production,
whereby the polycondensability is improved.
DISCLOSURE OF THE INVENTION
[0008] As its gist, the present invention provides a polyester
resin produced by polycondensing a dicarboxylic acid component
containing terephthalic acid or its ester-forming derivative as the
main component, and a diol component containing ethylene glycol as
the main component in the presence of (1) a compound of at least
one member selected from the group consisting of titanium group
elements in Group 4A of the periodic table, via an esterification
reaction or an ester exchange reaction, characterized in that the
content of copolymerized components other than the terephthalic
acid component and the ethylene glycol component, is not more than
4 mol % based on the total dicarboxylic acid component, and in a
molded product with a thickness of 3.5 mm injection-molded at
280.degree. C., the difference between the absorbance at a
wavelength of 395 nm and the absorbance at a wavelength of 800 nm
is at least 0.08, and the difference between the absorbance at a
wavelength of 500 nm and the absorbance at a wavelength of 800 nm
is at most 0.05.
[0009] Further, as its gist, the present invention provides a
process for producing a polyester resin, which comprises
polycondensing a dicarboxylic acid component containing
terephthalic acid or its ester-forming derivative as the main
component, and a diol component containing ethylene glycol as the
main component in the presence of (1) a compound of at least one
member selected from the group consisting of titanium group
elements in Group 4A of the periodic table, (2) a compound of at
least one element selected from the group consisting of metal
elements of Group 1A of the periodic table, elements of Group 2A of
the periodic table, manganese, iron and cobalt, and (3) a
phosphorus compound, via an esterification reaction or an ester
exchange reaction, characterized in that the amounts of the
respective compounds (1), (2) and (3) are such amounts that their
contents will be from 0.02 to 0.2 mol as the total amount (T) of
atoms of the compound (1), from 0.04 to 0.6 mol as the total amount
(M) of atoms of the compound (2) and from 0.02 to 0.4 mol as the
total amount (P) of atoms of the compound (3), per 1 ton of the
polyester resin.
BRIEF DESCRIPTION OF THE DRAWINGS
[0010] FIG. 1(a): a plan view of a stepped molded plate for
evaluation of the physical properties, molded in Examples.
[0011] FIG. 1(b): a front view of the stepped molded plate for
evaluation of the physical properties, molded in Examples.
BEST MODE FOR CARRYING OUT THE INVENTION
[0012] The polyester resin of the present invention is one produced
by polycondensing a dicarboxylic acid component containing
terephthalic acid or its ester-forming derivative as the main
component, and a diol component containing ethylene glycol as the
main component, via an esterification reaction or an ester exchange
reaction, and is preferably a polycondensate of a dicarboxylic acid
component in which the terephthalic acid component constitutes at
least 96 mol %, more preferably at least 99 mol %, of the total
dicarboxylic acid component, with a diol component in which the
ethylene glycol component constitutes at least 96 mol %, more
preferably at least 97 mol %, of the total diol component. If the
proportion of the terephthalic acid component in the total
dicarboxylic acid component, and the proportion of the ethylene
glycol component in the total diol component, are less than the
above ranges, the aligned crystallization of the molecular chains
by stretching at the time of molding a bottle, etc., tends to be
inadequate, whereby the mechanical strength, the gas barrier
property, the heat resistance, etc., as a molded product such as a
bottle, tend to be inadequate.
[0013] And, in the polyester resin of the present invention, it is
essential that the content of copolymerizable components other than
the terephthalic acid component and the ethylene glycol component
is not more than 4 mol %, preferably not more than 3 mol %, further
preferably not more than 2 mol %. If the content of copolymerizable
components exceeds the above range, it tends to be difficult to
obtain a molded product which is excellent in e.g. the
aroma-retention property, etc., and in which the acetaldehyde
content is reduced.
[0014] Further, the ester-forming derivative of terephthalic acid
may, for example, be a C.sub.1-4 alkyl ester, a halogenated
product, etc. Further, dicarboxylic acid components other than
terephthalic acid or its ester-forming derivative, may, for
example, be an aromatic dicarboxylic acid such as phthalic acid,
isophthalic acid, dibromoisophthalic acid, sodium
sulfoisophthalate, phenylene dioxydicarboxylic acid, 4,4'-diphenyl
dicarboxylic acid, 4,4'-diphenyl ether dicarboxylic acid,
4,4'-diphenyl ketone dicarboxylic acid, 4,4'-diphenoxyethane
dicarboxylic acid, 4,4'-diphenylsulfone dicarboxylic acid or
2,6-naphthalene dicarboxylic acid, an alicyclic dicarboxylic acid
such as hexahydroterephthalic acid or hexahydroisophthalic acid,
and an aliphatic dicarboxylic acid such as succinic acid, glutaric
acid, adipic acid, pimelic acid, suberic acid, azelaic acid,
sebacic acid, undecadicarboxylic acid or dodecacarboxylic acid, as
well as a C.sub.1-4 alkyl ester thereof, and a halogenated product
thereof. Among them, in the present invention, isophthalic acid or
its ester-forming derivative is preferred, and the proportion in
the total dicarboxylic acid component is preferably from 0.1 to 3
mol %. If isophthalic acid is within this range, the solid phase
polycondensation rate is high, and reduction of the acetaldehyde
content in a molded product of the obtainable resin tends to be
facilitated.
[0015] Further, as the diol component other than ethylene glycol,
diethylene glycol formed as a by-product in the reaction system may
be mentioned, and the proportion of such diethylene glycol in the
total diol component is preferably not more than 3 mol %, more
preferably from 1 to 3 mol %, inclusive of one added as a
copolymerizable component from outside the system. If diethylene
glycol exceeds this range, a problem tends to occur such that when
the obtainable resin is formed into a molded product, the gas
barrier property decreases, or it tends to be difficult to reduce
the acetaldehyde content. Further, other diol components may, for
example, be an aliphatic diol such as trimethylene glycol,
tetramethylene glycol, pentamethylene glycol, hexamethylene glycol,
octamethylene glycol, decamethylene glycol, neopentyl glycol,
2-ethyl-2-butyl-1,3-propane diol, polyethylene glycol or
polytetramethylene ether glycol, an alicyclic diol such as
1,2-cyclohexanediol, 1,4-cyclohexanediol,
1,1-cyclohexanedimethylol, 1,4-cyclohexanedimethylol or
2,5-norbornanedimethylol, and an aromatic diol such as xylylene
glycol, 4,4'-dihydroxybiphenyl, 2,2-bis(4'-hydroxyphenyl)propane,
2,2-bis(4'-.beta.-hydroxyethoxyphenyl)propane,
bis(4-hydroxyphenyl)sulfone or
bis(4-.beta.-hydroxyethoxyphenyl)sulfonic acid, as well as an
ethylene oxide adduct or a propylene oxide adduct, of
2,2-bis(4'-hydroxyphenyl)propane.
[0016] Further, copolymerizable components may, for example, be a
hydroxycarboxylic acid or an alkoxycarboxylic acid, such as
glycolic acid, p-hydroxybenzoic acid or
p-.beta.-hydroxyethoxybenzoic acid, a single functional component
such as stearyl alcohol, heneycosanol, octacosanol, benzyl alcohol,
stearic acid, behenic acid, benzoic acid, t-butyl benzoic acid or
benzoylbenzoic acid, and a polyfunctional component with at least
trifunctional, such as tricarbarylic acid, trimellitic acid,
trimesic acid, pyromellitic acid, naphthalene tetracarboxylic acid,
gallic acid, trimethylolethane, trimethylolpropane, glycerol,
pentaerythritol or sugar ester.
[0017] The polyester resin of the present invention is such that in
a molded product with a thickness of 3.5 mm injection-molded at
280.degree. C., the difference between the absorbance at a
wavelength of 395 nm and the absorbance at a wavelength of 800 nm
is at least 0.08, and this difference in absorbance is preferably
at least 0.15, more preferably at least 0.20. If this difference in
absorbance is less than the above range, it tends to be difficult
to obtain a molded product excellent in the ultraviolet shielding
property. Further, in a molded product having a thickness of 3.5 mm
injection-molded at 280.degree. C., the difference between the
absorbance at a wavelength of 500 nm and the absorbance at a
wavelength of 800 nm is at most 0.05, and this difference in
absorbance is preferably at most 0.04, more preferably at most
0.03. If this difference in absorbance is less than the above
range, it tends to be difficult to obtain a molded product
excellent in the color tone. Here, the absorbance of a molded
product is a value at each wavelength when measured by means of an
ultraviolet visible light absorption photometer within a wavelength
range of from 300 to 800 nm at a scanning speed of 127 nm/min.
[0018] Further, the polyester resin of the present invention is
such that the temperature-rising crystallization temperature (Tc)
of the resin in the molded product after the injection molding at
280.degree. C., is preferably from 150 to 180.degree. C., more
preferably from 155 to 165.degree. C., particularly preferably from
157 to 164.degree. C. This temperature-rising crystallization
temperature (Tc) relates to the crystallization rate of the mouth
stopper portion, etc. at the time of molding a bottle, and if the
temperature-rising crystallization temperature (Tc) is either less
than the above range or more than the above range, the dimensional
stability at the mouth stopper portion deteriorates as a bottle,
and a problem such as leakage of a gas from the mouth stopper
portion or deterioration of the aroma-retention property, tends to
result. Here, the temperature-rising crystallization temperature
(Tc) is one obtained by measuring the crystallization peak
temperature observed in the temperature rise when the temperature
was raised from 20.degree. C. to 285.degree. C. at a rate of
20.degree. C./min in a nitrogen stream by means of a differential
scanning calorimeter.
[0019] Further, the polyester resin of the present invention is
such that the intrinsic viscosity ([.eta.]) is preferably from 0.70
to 0.90 dl/g, more preferably from 0.70 to 0.80 dl/g, as a value
measured at 30.degree. C. in a solution in a mixed solvent of
phenol/tetrachloroethane (weight ratio: 1/1). If the intrinsic
viscosity ([.eta.]) is less than the above range, the mechanical
strength tends to be inadequate as a molded product such as a
bottle. On the other hand, if it exceeds the above range, the
moldability for a bottle or the like tends to deteriorate, and it
tends to be difficult to control production of acetaldehyde, etc.
as by-products at the time of the melt molding. Further, as the
color tone, the color coordinate value b of the Hunter's color
difference formula in the Lab color system as disclosed in
Reference 1 in JIS Z8730, is preferably not more than 4, more
preferably from -5 to 2. If value b exceeds the above range, the
color tone tends to be yellowish as a molded product such as a
bottle. Further, the cyclic trimer content (CT) is preferably not
more than 0.50 wt %, more preferably not more than 0.40 wt %. If
the cyclic trimer content (CT) exceeds the above range,
contamination of the mold tends to occur during molding of a
bottle, etc.
[0020] Further, the acetaldehyde content (AA.sub.1) is preferably
not more than 5.0 ppm, more preferably not more than 3.0 ppm.
Further, the acetaldehyde content (AA.sub.2) of the resin in a
molded product after injection-molded at 280.degree. C., is
preferably not more than 20 ppm, more preferably not more than 18
ppm, particularly preferably not more than 15 ppm. If the
acetaldehyde content (AA.sub.1) and the acetaldehyde content
(AA.sub.2) exceed the above ranges, it tends to be difficult to
eliminate an influence over the taste, the aroma, etc. of the
content, as a molded product such as bottle. Further, the haze of a
molded product with a thickness of 5 mm after the injection molding
at 280.degree. C. is preferably not more than 10%, more preferably
not more than 8%.
[0021] And, in the present invention, in order to bring the
above-mentioned content of copolymerizable components, the
intrinsic viscosity ([.eta.]), color coordinate value b, the cyclic
trimer content (CT), the acetaldehyde content (AA.sub.1), as well
as the absorbance of the molded product after the injection molding
at 280.degree. C., the temperature-rising crystallization
temperature (Tc), the acetaldehyde content (AA.sub.2), and the
haze, etc. within the above ranges, it is essential that the
polycondensation of the polyester resin is carried out in the
presence of (1) a compound of at least one member selected from the
group consisting of titanium group elements in Group 4A of the
periodic table. Accordingly, the polyester resin of the present
invention contains (1) a compound of at least one member selected
from the group consisting of titanium group elements in Group 4A of
the periodic table.
[0022] Here, (1) the compound of a titanium group element of Group
4A of the periodic table, i.e. titanium, zirconium or hafnium, may,
for example, be an oxide, a hydroxide, an alkoxide, an acetate, a
carbonate, a oxalate and a halide of such an element. Among
compounds of such elements, a titanium compound is preferred.
Specifically, the titanium compound may, for example, be a titanium
alkoxide such as tetra-n-propyl titanate, tetra-i-propyl titanate,
tetra-n-butyl titanate, tetra-n-butyl titanate tetramer,
tetra-t-butyl titanate, tetracyclohexyl titanate, tetraphenyl
titanate or tetrabenzyl titanate, a titanium oxide obtainable by
the hydrolysis of a titanium alkoxide, a titanium/silicon or
zirconium double oxide obtainable by the hydrolysis of a mixture of
a titanium alkoxide with a silicon alkoxide or a zirconium
alkoxide, titanium acetate, titanium oxalate, titanium potassium
oxalate, titanium sodium oxalate, potassium titanate, sodium
titanate, a titanic acid/aluminum hydroxide mixture, titanium
chloride, a titanium chloride/aluminum chloride mixture, titanium
bromide, titanium fluoride, potassium hexafluorotitanate, cobalt
hexafluorotitanate, manganese hexafluorotitanate, ammonium
hexafluorotitanate, or titanium acetylacetonate. Among them, a
titanium alkoxide such as tetra-n-propyl titanate, tetra-i-propyl
titanate or tetra-n-butyl titanate, titanium oxalate or titanium
potassium oxalate, is preferred, and tetra-n-butyl titanate is
particularly preferred.
[0023] Further, with respect to the polycondensation, from the
viewpoint of the polycondensability, reduction of by-products such
as acetaldehyde, a cyclic trimer, etc. in the obtainable resin and
the color tone, as well as the absorbance of the molded product,
the temperature-rising crystallization temperature, etc., one
polycondensed in the coexistence of (2) a compound of at least one
element selected from the group consisting of metal elements of
Group 1A of the periodic table, elements of Group 2A of the
periodic table, manganese, iron and cobalt, and (3) a phosphorus
compound, is preferred. Accordingly, the polyester resin of the
present invention preferably contains (2) the compound of at least
one element selected from the group consisting of metal elements of
Group 1A of the periodic table, elements of Group 2A of the
periodic table, manganese, iron and cobalt, and (3) the phosphorus
compound.
[0024] Here, (2) the compound of at least one element selected from
the group consisting of metal elements of Group 1A of the periodic
table, elements of Group 2A of the periodic table, manganese, iron
and cobalt, may, for example, be an oxide, a hydroxide, an
alkoxide, an acetate, a carbonate, an oxalate, a halide, etc. of
lithium, sodium, potassium, magnesium, calcium, manganese, iron,
cobalt, etc. Specifically, it may, for example, be lithium acetate,
sodium acetate, potassium acetate, magnesium oxide, magnesium
hydroxide, magnesium alkoxide, magnesium acetate, magnesium
carbonate, calcium oxide, calcium hydroxide, calcium acetate,
calcium carbonate, manganese oxide, manganese hydroxide, manganese
acetate, ferric acetate, cobalt formate, cobalt acetate, cobalt
oxalate, cobalt carbonate, cobalt bromide or cobalt
acetylacetonate. Among them, a magnesium compound or a manganese
compound is preferred. Particularly preferred is a magnesium
compound, and magnesium acetate is especially preferred.
[0025] Further, (3) the phosphorus compound may, specifically, be a
pentavalent phosphorus compound, such as orthophosphoric acid,
polyphosphoric acid or a phosphoric acid ester such as trimethyl
phosphate, triethyl phosphate, tri-n-butyl phosphate, trioctyl
phosphate, triphenyl phosphate, tricresyl phosphate,
tris(triethylene glycol) phosphate, methyl acid phosphate, ethyl
acid phosphate, isopropyl acid phosphate, butyl acid phosphate,
monobutyl phosphate, dibutyl phosphate, dioctyl phosphate or
triethylene glycol acid phosphate, phosphorous acid,
hypophosphorous acid, a phosphorous acid ester such as trimethyl
phosphite, diethyl phosphite, triethyl phosphite, trisdodecyl
phosphite, trisnonyldecyl phosphite, ethyl diethyl phosphonoacetate
or triphenyl phosphite, or a trivalent phosphorus compound such as
a metal salt of lithium, sodium, potassium, etc. Among them, a
phosphoric acid ester as a pentavalent phosphorus compound is
preferred. Particularly preferred is trimethyl phosphate or ethyl
acid phosphate.
[0026] In the present invention, the respective amounts of (1) the
above compound of at least one member selected from the group
consisting of titanium group elements in Group 4A of the periodic
table, (2) the above compound of at least one element selected from
the group consisting of metal elements of Group 1A of the periodic
table, elements of Group 2A of the periodic table, manganese, iron
and cobalt, and (3) the above phosphorus compound, used at the time
of polycondensation, and the respective contents in the resulting
polyester resin, are preferably from 0.002 to 1 mol, more
preferably from 0.002 to 0.5 mol, as the total amount (T) of atoms
of the compound (1), preferably from 0.04 to 5 mol, more preferably
from 0.04 to 3 mol, as the total amount (M) of atoms of the
compound (2), and preferably from 0.02 to 4 mol, more preferably
from 0.02 to 2 mol, as the total amount (P) of atoms of the
compound (3), per 1 ton of the polyester resin.
[0027] When the total amount (T) of atoms of the compound (1), the
total amount (M) of atoms of the compound (2) and the total amount
(P) of atoms of the compound (3) are within the above ranges, the
ultraviolet shielding properties tend to be excellent. Further,
particularly, in order to reduce the acetaldehyde content in the
molded product and to improve the polycondensability, the total
amount (T) of atoms of the compound (1) is more preferably from
0.02 to 0.2 mol, particularly preferably from 0.04 to 0.15 mol, the
total amount (M) of atoms of the compound (2) is more preferably
from 0.04 to 0.6 mol, particularly preferably from 0.05 to 0.4 mol,
most preferably from 0.1 to 0.3 mol, and the total amount (P) of
atoms of the compound (3) is more preferably from 0.02 to 0.4 mol,
particularly preferably from 0.1 to 0.0.3 mol, per 1 ton of the
polyester resin.
[0028] Further, once the amounts of the respective compounds i.e.
(1) the compound of at least one member selected from the group
consisting of titanium group elements in Group 4A of the periodic
table, (2) the compound of at least one element selected from the
group consisting of metal elements of Group 1A of the periodic
table, elements of Group 2A of the periodic table, manganese, iron
and cobalt, and (3) the phosphorus compound, satisfy the molar
amounts of the above ranges as the total amount (T) of atoms of the
compound (1), as the total amount (M) of atoms of the compound (2),
and as the total amount (P) of atoms of the compound (3), it is
preferred that the molar ratio [P/T] of the total amount (P) of
atoms of the compound (3) to the total amount (T) of atoms of the
compound (1) is from 0.1 to 10, more preferably from 1 to 7,
particularly preferably from 2 to 5, and the molar ratio [M/T] of
the total amount (M) of atoms of the compound (2) to the total
amount (T) of atoms of the compound (1) is from 0.1 to 10, more
preferably from 0.5 to 7, particularly preferably from 3 to 5.
Further, for a polyester resin particularly excellent in the
ultraviolet shielding property, it is preferred that the molar
ratio [P/M] of the total amount (P) of atoms of the compound (3) to
the total amount (M) of atoms of the compound (2), is more than 0
to 10, more preferably from 1 to 5, particularly preferably from 2
to 4, and the molar ratio [P/(T+M)] of the total amount (P) of
atoms of the compound (3) to the sum of the total amount (T) of
atoms of the compound (1) and the total amount (M) of atoms of the
compound (2), is more than 0 to 10, more preferably from 0.5 to 5,
particularly preferably from 1 to 3.
[0029] If the molar ratio [P/T] is less than the above range, the
obtainable resin tends to be yellowish, and thus the color tone
tends to deteriorate. On the other hand, if it exceeds the above
range, the melt polycondensability and the solid phase
polycondensability, which will be described hereinafter, tend to
deteriorate simultaneously. Further, if the above molar ratio [M/T]
is less than the above range, the melt polycondensability and the
solid phase polycondensability, which will be described
hereinafter, will deteriorate simultaneously, and it tends to be
difficult to reduce the acetaldehyde content in the molded product
of the resulting resin. On the other hand, if it exceeds the above
range, the solid phase polycondensability which will be described
hereinafter, tends to deteriorate.
[0030] Further, in the present invention, during the
polycondensation, metal compounds other than the above-mentioned
respective compounds, may be present within a range not to impair
the effects of the present invention, and accordingly, such metal
compounds may be contained in the polyester resin of the present
invention. In such a case, the metal compounds may, for example, be
compounds such as oxides, hydroxides, alkoxides, carbonates,
phosphates, carboxylates or halides of aluminum, chromium, nickel,
copper, zinc, germanium, molybdenum, silver, tin, lanthanum,
cerium, tungsten, gold, etc. The above-mentioned respective
compounds and other compounds are preferably ones soluble in water
or an alcohol such as ethylene glycol.
[0031] The polyester resin of the present invention is produced by
polycondensing a dicarboxylic acid component containing the above
terephthalic acid or its ester-forming derivative as the main
component and a diol component containing ethylene glycol as the
main component in the presence of (1) the compound of at least one
element selected from the group consisting of titanium group
elements of Group 4A of the periodic table, preferably in the
coexistence of (2) the compound of at least one element selected
from the group consisting of metal elements of Group 1A of the
periodic table, elements of Group 2A of the periodic table,
manganese, iron and cobalt, and (3) the phosphorus compound, via an
esterification reaction or an ester exchange reaction, but
basically in accordance with a common process for producing a
polyester resin. Namely, it is produced by introducing into a
slurry preparation tank the above dicarboxylic acid component
containing the above terephthalic acid or its ester-forming
derivative as the main component and the diol component containing
ethylene glycol as the main component together with optional
copolymerizable components, etc., followed by mixing with stirring
to obtain a raw material slurry, subjecting it to an esterification
reaction for from about 1 to 10 hours in an esterification reactor
under atmospheric pressure or elevated pressure under heating with
stirring or to an ester exchange reaction in the presence of an
ester exchange catalyst, then transferring the obtained polyester
low molecular weight product as the esterification reaction product
or the ester exchange reaction product to a polycondensation tank,
and melt polycondensing it in the presence of the above-mentioned
compounds under atmospheric pressure or gradually reduced pressure
under heating with stirring for about 1 to 20 hours. These
operations may be carried out by a continuous system or by a batch
system.
[0032] At that time, preparation of the raw material slurry
comprising the dicarboxylic acid component containing terephthalic
acid or its ester-forming derivative as the main component and the
diol component containing ethylene glycol as the main component, is
carried out preferably by adjusting the molar ratio of the total
diol component to the total dicarboxylic acid component to be
within a range of from 1.0 to 2.5, more preferably within a range
of from 1.03 to 1.7.
[0033] Further, the esterification reaction is carried out by means
of a single esterification reactor or a multi-stage reaction
apparatus having a plurality of esterification reactors connected
in series, under reflux of ethylene glycol, while removing water
formed by the reaction and excess ethylene glycol out of the
system. At that time, the esterification ratio (the proportion of
the esterified by a reaction with the diol component among the
total carboxyl groups of the raw material dicarboxylic acid
component) of the polyester low molecular weight product as the
esterification reaction product or the ester exchange reaction
product, is preferably at least 95%. Further, the number average
molecular weight of the low molecular weight product is preferably
from 500 to 5,000. Further, in the case of the ester exchange
reaction, it is necessary to employ an ester exchange catalyst,
whereby the transparency of the resulting resin usually tends to be
poor. Accordingly, in the present invention, the product is
preferably one produced via the esterification reaction.
[0034] With respect to the reaction conditions in the
esterification reaction, in the case of a single esterification
reactor, the temperature is usually at a level of from 240 to
280.degree. C., the relative pressure to the atmosphere is usually
at a level of from 0 to 400 kPa (from 0 to 4 kg/cm.sup.2G), and the
reaction time is from about 1 to 10 hours with stirring. In the
case of a plurality of esterification reactors, the reaction
temperature in the esterification reactor for the first stage is
usually from 240 to 270.degree. C., preferably from 245 to
265.degree. C., and the relative pressure to the atmospheric
pressure is usually from 5 to 300 kPa (from 0.05 to 3
kg/cm.sup.2G), preferably from 10 to 200 kPa (from 0.1 to 2
kg/cm.sup.2G), and the reaction temperature in the final stage is
usually from 250 to 280.degree. C., preferably from 255 to
275.degree. C., and the relative pressure to the atmospheric
pressure is usually from 0 to 150 kPa (from 0 to 1.5 kg/cm.sup.2G),
preferably from 0 to 130 kPa (from 0 to 1.3 kg/cm.sup.2G). Further,
the esterification ratio in each stage is preferably adjusted so
that its increase will be equal.
[0035] Further, in the esterification reaction, it is possible to
suppress production of diethylene glycol as a by-product from
ethylene glycol, by adding a small amount of e.g. a tertiary amine
such as triethylamine, tri-n-butylamine or benzyl dimethylamine, a
quaternary ammonium hydroxide such as tetraethylammonium hydroxide,
tetra-n-butylammonium hydroxide or trimethylbenzylammonium
hydroxide, or a basic compound such as lithium carbonate, sodium
carbonate, potassium carbonate or sodium acetate.
[0036] Further, the melt polycondensation is carried out under
reduced pressure, while distilling off formed ethylene glycol out
of the system, by means of a single melt polymerization tank, or a
multi-stage reaction apparatus having a plurality of melt
polycondensation tanks connected in series, for example, an
apparatus comprising a perfect mixing type reactor equipped with
stirring vanes for the first stage and horizontal plug flow type
reactors equipped with stirring vanes for the second and third
stages.
[0037] With respect to the reaction conditions in the melt
polycondensation, in the case of a single polycondensation tank,
the temperature is usually from about 250 to 290.degree. C., the
pressure is gradually reduced from the atmospheric pressure, so
that finally, the absolute pressure will be usually at a level of
from 1.3 to 0.013 kPa (from 10 to 0.1 Torr), and the reaction time
is from about 1 to 20 hours with stirring. Whereas, in the case of
a plurality of polycondensation tanks, the reaction temperature in
the polycondensation tank for the first stage is usually from 250
to 290.degree. C., preferably from 260 to 280.degree. C. and the
absolute pressure is usually from 65 to 1.3 kPa (from 500 to 10
Torr), preferably from 26 to 2 kPa (from 200 to 15 Torr), and the
reaction temperature in the final stage is usually from 265 to
300.degree. C., preferably from 270 to 295.degree. C., and the
absolute pressure is usually from 1.3 to 0.013 kPa (from 10 to 0.1
Torr), preferably from 0.65 to 0.065 kPa (from 5 to 0.5 Torr). The
reaction conditions for an intermediate stage are selected to be
intermediate conditions thereof, and for example, in a three stage
reaction apparatus, the reaction temperature in the second stage is
usually from 265 to 295.degree. C., preferably from 270 to
285.degree. C., and the absolute pressure is usually from 6.5 to
0.13 kPa (from 50 to 1 Torr), preferably from 4 to 0.26 kPa (from
30 to 2 Torr).
[0038] Further, at the time of polycondensation, timing for
addition of (1) the compound of at least one element selected from
the group consisting of titanium group elements of Group 4A of the
periodic table, (2) the compound of at least one element selected
from the group consisting of metal elements of Group 1A of the
periodic table, elements of Group 2A of the periodic table,
manganese, iron and cobalt, and (3) the phosphorus compound, to the
reaction system, may be at any one of an optional stage of a step
of preparing a slurry of the starting material terephthalic acid or
its ester-forming derivative, ethylene glycol, and optionally
employed other dicarboxylic acid components, or a step of the
esterification reaction or the ester exchange reaction, or in the
initial stage of the melt polycondensation step. However, the
compounds (1) and (2) are added preferably in the step of the
esterification reaction or the ester exchange reaction, or in the
stage of transportation to the melt polycondensation step, and it
is also preferred that they are added at a stage where the
esterification ratio of the esterification reaction product or the
ester exchange reaction product reaches at least 90%. Further, it
is preferred that the compound (1) is added later than the compound
(2). Further, it is preferred that the compound (3) is added at a
stage where the esterification ratio of the esterification reaction
product or the ester exchange reaction product is less than
90%.
[0039] With respect to the specific steps for addition of the
respective compounds, it is preferred, for example, that the
compound (1) is added to the esterification reaction tank for the
final stage in the multi-stage reaction apparatus or to the
esterification reaction product or the ester exchange reaction
product in the stage for transportation to the melt
polycondensation step, and the compound (2) is added to the
esterification reaction tank for the final stage in the multi-stage
reaction apparatus. Further, the compound (3) is preferably added
to the slurry preparation tank or the esterification reaction tank
for the first stage, particularly preferably to the slurry
preparation tank. Namely, in the present invention, it is preferred
to set the order of addition of the respective compounds (1), (2)
and (3) to the reaction system to be (3) then (2) and then (3).
[0040] By setting the timing of addition and the order of addition
of the respective compounds (1), (2) and (3) to the reaction system
as mentioned above, the thermal stability of the resin can be
improved, and production of diethylene glycol as a by-product in
the reaction system which causes production of acetaldehyde, etc.
as by-products during the melt molding, can be suppressed, and
further, it is possible to effectively obtain the effects for
improving the melt polycondensability and the solid phase
polycondensability.
[0041] Further, addition of the respective compounds (1), (2) and
(3) to the reaction system at the time of the polycondensation, is
preferably carried out in the form of a solution in e.g. water or
an alcohol such as ethylene glycol. In an ethylene glycol solution
in a case where a titanium compound is used as the compound (1), it
is preferred to adjust the concentration of titanium atoms to be
from 0.01 to 0.3 wt % and the water concentration to be from 0.1 to
1 wt %, from the viewpoint of the dispersibility of the titanium
compound in the reaction system and the improvement of the melt
polycondensability and the solid phase polycondensability thereby
obtainable.
[0042] Further, the reaction time for the melt polycondensation is
usually preferably at most 3.5 hours. If the reaction time exceeds
it, it tends to be difficult to reduce the aldehyde content in the
resulting resin and the amount of acetaldehyde by-product during
the melt molding.
[0043] The polyester resin obtainable by the above melt
polycondensation is such that the intrinsic viscosity
([.eta..sub.1]) is preferably from 0.35 to 0.75 dl/g, more
preferably from 0.50 to 0.60 dl/g, as a value measured at
30.degree. C. in a solution in a mixed solvent of
phenol/tetrachloroethane (weight ratio: 1/1). If the intrinsic
viscosity ([.eta..sub.1]) is less than the above range, the
withdrawing property from the polycondensation tank, which will be
described hereinafter, tends to be poor. On the other hand, if it
exceeds the above range, it tends to be difficult to reduce the
acetaldehyde content in the resulting resin. Further, the melt
polycondensation velocity (V.sub.1) as a value obtained by dividing
the above-mentioned intrinsic viscosity ([.eta..sub.1]) of the
resulting polyester resin by the above-mentioned reaction time, is
preferably at least 0.15 dl/g/hr.
[0044] Further, the resin obtained by the melt polycondensation is
usually withdrawn in the form of a strand from a discharge outlet
provided at the bottom of the polycondensation tank and, while
being cooled by water or after being cooled by water, cut by a
cutter into particles such as pellets or chips. Further, such
particles after the melt polycondensation, are usually heated at a
temperature of from about 60 to 180.degree. C. in an atmosphere of
an inert gas such as nitrogen, carbon dioxide or argon, or in a
steam atmosphere, or in a steam-containing inert gas atmosphere, to
crystallize the surface of the resin particles and then subjected
to solid phase polycondensation by heat treatment at a low
temperature of from immediately below the adhesive temperature of
the resin to 80.degree. C. in an inert gas atmosphere or/and under
a reduced pressure of from 1.3 to 0.013 kPa (from 10 to 0.1 Torr),
usually for a period of at most 50 hours, while letting the
particles flow not to fuse one another. By this solid phase
polycondensation, it is possible to further increase the
polymerization degree and to reduce by-products such as
acetaldehyde, a cyclic trimer, etc.
[0045] The polyester resin obtainable by the above solid phase
polycondensation is such that the intrinsic viscosity
([.eta..sub.2]) is preferably from 0.70 to 0.90 dl/g, more
preferably from 0.70 to 0.80 dl/g, as a value measured at
30.degree. C. in a solution in a mixed solvent of
phenol/tetrachloroethane (weight ratio: 1/1). Further, the solid
phase polycondensation velocity (V.sub.2) as a value obtained by
dividing the difference ([.eta..sub.2]-[.eta..sub.1]) between the
above intrinsic viscosity ([.eta..sub.2]) of the obtainable solid
phase polycondensation resin and the intrinsic viscosity
([.eta..sub.1]) of the above-mentioned melt polycondensation resin,
by the above-mentioned reaction time, is preferably from 0.008 to
0.015 dl/g/hr. Further, the ratio (V.sub.2/V.sub.1) of this solid
phase polycondensation velocity to the above-mentioned melt
polycondensation velocity is preferably within a range of from 0.04
to 0.07, more preferably within a range of from 0.05 to 0.07.
[0046] Further, for the purpose of improving the thermal stability,
reduction of by-products such as acetaldehyde, a cyclic trimer,
etc. during the molding, etc., the resin obtained by the above melt
polycondensation or the solid phase polycondensation may usually be
subjected to water treatment of dipping it in warm water of at
least 40.degree. C. for at least 10 minutes, or steam treatment of
contacting it with steam or a steam-containing gas of at least
60.degree. C. for at least 30 minutes, or treatment with an organic
solvent, an acidic aqueous solution of e.g. various mineral acids,
organic acids or phosphoric acids, or treatment by an alkaline
aqueous solution or an organic solvent solution, of a Group 1A
metal, a Group 2A metal or an amine.
[0047] Further, the polyester resin of the present invention may
contain a crystalline thermoplastic resin different from the
polyester resin in a content of from 0.0001 to 1,000 ppm,
preferably from 0.0005 to 100 ppm, more preferably from 0.001 to 10
ppm, as the case requires, to adjust the temperature-rising
crystallization temperature (Tc) of the resin in the
above-mentioned molded product after injection molding to the
above-mentioned range. As such a crystalline thermoplastic resin, a
polyolefin resin or a polyamide resin may be mentioned as a typical
example.
[0048] The polyolefin resin may, for example, be a homopolymer of
an .alpha.-olefin having from about 2 to 8 carbon atoms, such as
ethylene, propylene or butene-1, or a copolymer of such an
.alpha.-olefin with another .alpha.-olefin having from 2 to 20
carbon atoms such as ethylene, propylene, 1-butene,
3-methyl-1-butene, 1-pentene, 4-methyl-1-pentene, 1-hexene,
1-octene or 1-decene, or with a vinyl compound such as vinyl
acetate, acrylic acid, methacrylic acid, an acrylate, a
methacrylate, vinyl chloride or styrene. Specifically, it may, for
example, be an ethylene resin such as an ethylene homopolymer such
as a low, intermediate or high density polyethylene, an
ethylene/propylene copolymer, an ethylene/1-butene copolymer, an
ethylene/4-methyl-1-pentene copolymer, an ethylene/1-hexene
copolymer, an ethylene/1-octene copolymer, an ethylene/vinyl
acetate copolymer, an ethylene/acrylic acid copolymer, an
ethylene/methacrylic acid copolymer or an ethylene/ethyl acrylate
copolymer, a propylene resin such as a propylene homopolymer, a
propylene/ethylene copolymer or a propylene/ethylene/1-butene
copolymer, and a 1-butene resin such as a 1-butene homopolymer, a
1-butene/ethylene copolymer or a 1-butene/propylene copolymer.
[0049] Further, the polyamide resin may, for example, be a polymer
of a lactam such as butyrolactam, .delta.-valerolactam,
.epsilon.-caprolactam, enantholactam or .omega.-lauryllactam, a
polymer of an amino acid such as 6-amino caproic acid, 7-amino
heptanoic acid, 8-amino octanoic acid, 9-amino nonanoic acid,
11-amino undecanoic acid or 12-amino dodecanoic acid, a
polycondensate of a diamine, such as an aliphatic diamine such as
1,4-butane diamine, 1,5-pentane diamine, 1,5-hexane diamine,
1,6-hexane diamine, 1,9-nonane diamine, 1,11-undeca diamine,
1,12-dodecane diamine or .alpha.,.omega.-diaminopolypropylene
glycol, an alicyclic diamine such as 1,3- or
1,4-bis(aminomethyl)cyclohexane or bis(p-aminocyclohexylmethane),
or an aromatic diamine such as m- or p-xylylene diamine, with a
dicarboxylic acid, such as an aliphatic dicarboxylic acid such as
glutaric acid, adipic acid, suberic acid, sebacic acid or
dodecanoic diacid, an alicyclic dicarboxylic acid such as
cyclohexane dicarboxylic acid, or an aromatic dicarboxylic acid
such as terephthalic acid or isophthalic acid, or a copolymer
thereof. Specifically, for example, 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
6/66, nylon 6/610, nylon 6/12, nylon 6/6T or nylon 6I/6T may be
mentioned.
[0050] In the present invention, the above crystalline
thermoplastic resin may be incorporated to the polyester resin by a
common method such as a method of directly adding and melt mixing
or a method of adding and melt mixing as a master batch the above
crystalline thermoplastic resin to the above polyester resin so
that its content becomes within the above-mentioned range.
Otherwise, a method may be employed wherein the above crystalline
thermoplastic resin is directly added as a powder at a production
stage of the above polyester resin, for example, at any stage of
e.g. during the melt polycondensation (the starting materials,
slurry, catalyst, etc.), immediately after the melt
polycondensation, immediately after the preliminary
crystallization, during the solid phase polycondensation or
immediately after the solid phase polycondensation, or during a
period after the production stage until the molding stage, or a
liquid such as water having the powder dispersed therein, is
contacted with the polyester resin chips, a gas such as air having
the powder included, is contacted with the polyester resin chips,
or the polyester resin chips are contacted to a component made of
the crystalline thermoplastic resin under a flowing condition,
followed by melt kneading. Among the latter methods, a method is
preferred in which the crystalline thermoplastic resin is
incorporated to air for pneumatic transportation at the time of
pneumatic transportation to a preliminary crystallization machine
or at the time of pneumatic transportation to a solid
polycondensation tank, of chips of the polyester resin after the
melt polycondensation, or at the time of pneumatic transportation
to a storage tank or at the time of pneumatic transportation to a
molding machine, of chips after the solid phase
polycondensation.
[0051] Further, in the present invention, the polyester resin may
contain, for example, an ultraviolet absorber of e.g. a
benzophenone type such as 2,4-dihydroxybenzophenone,
2-hydroxy-4-methoxybenzophenone, 2-hydroxy-4-octoxybenzophenone,
2-hydroxy-4-dodecyloxybenzophenone,
2,2'-dihydroxy-4-methoxybenzophenone or
2,2'-dihydroxy-4,4'-dimethoxybenzophenone, a benzotriazole type
such as 2-(2'-hydroxy-5'-methylphenyl)benzotriazole,
2-(2'-hydroxy-5'-butylphenyl)benzotriazole,
2-(2'-hydroxy-5'-t-octylphenyl)benzotriazole,
2-(2'-hydroxy-3',5'-di-t-butylphenyl)benzotriazole,
2-(2'-hydroxy-3',5'-di-t-amylphenyl)benzotriazole,
2-(2'-hydroxy-3'-t-butyl-5'-methylphenyl)-5-chlorobenzotriazole or
2-(2'-hydroxy-3',5'-di-t-butylphenyl)-5-chlorobenzotriazole, a
salicylate type such as phenyl salicylate, p-t-butylphenyl
salicylate or p-octylphenyl salicylate, or a cyanoacrylate type
such as 2-ethylhexyl-2-cyano-3,3'-diphenylacryalte, and an
antioxidant, a photostabilizer, an antistatic agent, a lubricant, a
blocking preventive agent, an antifogging agent, a nucleating
agent, a plasticizer, a colorant, a filler, etc.
[0052] The polyester resin of the present invention may, for
example, be molded into a preform by injection molding, followed by
stretch blow molding, or molded into a parison by extrusion,
followed by blow molding, to obtain a bottle or the like, or it may
be formed into a sheet by extrusion, followed by heat forming to
obtain a tray, a container or the like, or said sheet may be
biaxially stretched to obtain a film or the like, which will be
particularly useful in the field of packaging beverage products.
Among them, it is particularly suitable for molding the preform
obtained by injection molding into a bottle by a biaxially
stretching blow molding method, and it is suitable, for example,
for a container for e.g. a carbonated beverage, an alcoholic
beverage, or a liquid seasoning such as soy sauce, a regular sauce,
Japanese sweet rice wine for cooking or dressing, or after heat
setting, for a container which is required to have an
aroma-retention property and an ultraviolet shielding property and
which is required to be free from an influence over the taste,
fragrance, etc., of a beverage such as a fruit juice beverage, a
vitamin beverage, a flavor tea or mineral water.
[0053] Now, the present invention will be described in further
detail with reference to Examples. However, the present invention
is by no means restricted by the following Examples.
EXAMPLE 1
[0054] Slurries of 43 kg (260 mol) of terephthalic acid and 19 kg
(312 mol) of ethylene glycol were continuously supplied over a
period of 4 hours to an esterification reaction tank having about
60 kg of bis(hydroxyethyl) terephthalate previously charged and
maintained at a temperature of 250.degree. C. and a pressure of
1.2.times.10.sup.5 Pa, and even after completion of the supply, the
esterification reaction was further carried out for one hour. About
one half of this esterification reaction product was transferred to
a polycondensation tank.
[0055] Then, to the polycondensation tank to which the
esterification reaction product was transferred, from its pipe,
ethyl acid phosphate, magnesium acetate and tetra-n-butoxy titanium
were sequentially added in their ethylene glycol solutions,
respectively, with intervals of 5 minutes, so that 0.387 mol of
phosphorus atoms (P), 0.062 mol of magnesium atoms (Mg) and 0.063
mol of titanium atoms (Ti) would remain per 1 ton of the resulting
polyester resin. Then, the interior of the system was heated from
250.degree. C. to 280.degree. C. over a period of 2 hours and 30
minutes, and at the same time, the pressure was reduced from normal
pressure to 4.times.10.sup.2 Pa over a period of one hour, and
while maintaining the same pressure, melt polycondensation was
carried out for a period of time until the intrinsic viscosity of
the obtained resin became 0.55 dl/g. The polymer was withdrawn in
the form of a strand from the discharge outlet provided at the
bottom of the polycondensation tank, cooled with water and then cut
into chips to obtain about 50 kg of a polyethylene terephthalate
resin.
[0056] Then, the obtained polyester resin chips were continuously
supplied into an agitation crystallizer maintained at about
160.degree. C. so that the retention time would be about 5 minutes,
for crystallization, then dried at 160.degree. C. for 2 hours in a
nitrogen stream of 40 l/min in an inert oven ("IPHH-201 model",
manufactured by ESPEC), and heated at 210.degree. C. for a period
of time until the intrinsic viscosity became 0.74 dl/g, for solid
phase polycondensation.
[0057] With respect to the obtained polyester resin chips, the
contents of copolymerizable components, the contents of metal atoms
of the respective metal compounds, the intrinsic viscosity
([.eta.]), the color coordinate value b as the color tone and the
cyclic trimer content (CT) were measured by the following methods,
and the results are shown in Table 1.
Content of Copolymerizable Component
[0058] With respect to a solution having a resin sample dissolved
at a concentration of 3 wt % in a mixed solvent of deuterated
chloroform/hexafluoroisopropanol (weight ratio: 7/3), .sup.1H-NMR
was measured by a nuclear magnetic resonance apparatus ("JNM-EX270
model", manufactured by Nippon Denshi K.K.), and the respective
peaks were identified, whereupon from the integral value of a peak,
the content of the copolymerizable component was calculated.
Contents of Metal Atoms
[0059] 2.5 g of a resin sample was ashed and completely decomposed
by hydrogen peroxide in the presence of sulfuric acid in accordance
with a usual method and then adjusted by distilled water to a
constant volume of 50 ml, and with respect to this sample,
quantitative analysis was carried out by means of a plasma emission
spectrometer (ICP-AES "JY46P model", manufactured by JOBIN YVON
COMPANY), whereupon the molar amount per 1 ton of the polyester
resin was calculated.
Intrinsic Viscosity ([.eta.])
[0060] 0.25 g of a freeze-pulverized resin sample was dissolved at
a concentration (c) of 1.0 g/dl in a mixed solvent of
phenol/tetrachloroethane (weight ratio: 1/1), at 110.degree. C. for
30 minutes in the case of a melt polycondensate resin, or at
120.degree. C. for 30 minutes in the case of a solid phase
polycondensate resin, whereupon by means of an Ubbellohde capillary
viscometer, the relative viscosity (.eta.rel) to the solvent was
measured at 30.degree. C. A ratio (.eta.sp/c) of the specific
viscosity (.eta.sp) obtained from this relative viscosity
(.eta.rel)-1, to the concentration (c), was obtained. In a similar
manner, the corresponding ratios (.eta.sp/c) were obtained when the
concentration (c) was changed to 0.5 g/dl, 0.2 g/dl and 0.1 g/dl,
respectively. From these values, a ratio (n sp/c) when the
concentration (c) was extrapolated to be 0, was obtained as the
intrinsic viscosity [.eta.] (dl/g)
Color Tone
[0061] A resin sample was filled into a cylindrical powder
calorimetric cell having an inner diameter of 36 mm and a depth of
15 mm to be flush, and by means of a calorimetric color difference
meter ("ND-300A", manufactured by NIPPON DENSHOKU INDUSTRIES CO.,
LTD.), color coordinate b of the Hunter's color difference formula
in the Lab color system as disclosed in Reference 1 of JIS Z8730,
was obtained as a simple average value of values measured at four
positions by rotating the cell every 90.degree. by a reflection
method.
Cyclic Trimer Content (CT)
[0062] 4.0 mg of a resin sample was accurately weighted and
dissolved in 2 ml of a mixed solvent of
chloroform/hexafluoroisopropanol (volume ratio: 3/2), and then
further diluted by an addition of 20 ml of chloroform. Then, 10 ml
of methanol was added thereto for reprecipitation, followed by
filtration to obtain a filtrate, which was evaporated to dryness.
Then, the residue was dissolved in 25 ml of dimethylformamide. The
amount of a cyclic trimer (cyclotriethylene terephthalate) in this
solution was quantitatively analyzed by liquid chromatography
("LC-10A", manufactured by Shimadzu Corporation).
[0063] Then, the obtained resin was dried at 160.degree. C. for at
least 16 hours in a vacuum dryer ("DP-41 model", manufactured by
YAMATO CHEMICAL INDUSTRY CO., LTD). Then, by an injection molding
machine ("M-70AII-DM", manufactured by Meiki Co., Ltd.), a stepped
molded plate having the shape as shown in FIG. 1 and having a size
of 50 mm.times.100 mm and thicknesses of six steps ranging from 6
mm to 3.5 mm in a transverse direction with each step being 0.5 mm,
was injection-molded at a cylinder temperature of 280.degree. C.
under a back pressure of 5.times.10.sup.5 Pa at an injection rate
of 40 cc/sec under a dwell pressure of 35.times.10.sup.5 Pa at a
mold temperature of 25.degree. C. and with a molding cycle of about
75 seconds. Further, in FIG. 1, G indicates a gate portion.
[0064] With respect to the molded plate thus obtained, the
absorbance at a wavelength of 395 nm and 500 nm, and the
temperature-rising crystallization temperature (Tc) were measured
by the following methods, and the results are shown in Table 1.
Absorbance
[0065] The portion having a thickness of 3.5 mm (portion A+B in
FIG. 1) in the molded plate, was measured by means of a ultraviolet
visible light spectrophotometer ("UV-2400", manufactured by
Shimadzu Corporation) at a scanning speed adjusted to be a low
speed mode (127 nm/min within a wavelength range of from 300 to 800
nm with a slit width of 5 nm at a sampling pitch of 0.5 nm by a
transmission mode, whereby the differences from the absorbance at a
wavelength of 800 nm, of the absorbances at wavelengths of 395 nm
and 500 nm, were obtained.
Temperature-Rising Crystallization Temperature (Tc)
[0066] The forward end portion (portion A in FIG. 1) having a
thickness of 3.5 mm in the molded plate, was cut out and dried at
40.degree. C. for 3 days by a vacuum dryer, whereupon a sample cut
out from the non-surface portion was used, and about 10 mg thereof
was accurately weighed and sealed in by means of an aluminum oven
pan and a pan cover (normal pressure type, "P/N SSC000E030" and
"P/N SSC000E032", manufactured by Seiko Denshi K.K.). By means of a
differential scanning calorimeter ("DSC220C", manufactured by Seiko
K.K.), the sample was heated from 20.degree. C. to 285.degree. C.
at a rate of 20.degree. C./min in a nitrogen stream, and the
crystallization peak temperature observed during the temperature
rise, was measured.
[0067] Separately, the obtained polyester resin chips were dried at
130.degree. C. for 10 hours by a vacuum dryer. Then, by an
injection molding machine ("FE-80S", manufactured by Nissei Plastic
Industrial Co., Ltd.), a preform of a test tube shape having an
outer diameter of 29.0 mm, a height of 165 mm, an average wall
thickness of 3.7 mm and a weight of 60 g, was injection-molded at a
cylinder temperature of 280.degree. C. under a back pressure of
5.times.10.sup.5 Pa at an injection rate of 45 cc/sec under a dwell
pressure of 30.times.10.sup.5 Pa at a mold temperature of
20.degree. C. with a molding cycle of about 4.0 seconds.
[0068] Such preforms were heated for 70 seconds in a near infrared
ray irradiation furnace equipped with a quartz heater, then left at
room temperature for 25 seconds and then introduced into a blow
mold set at 160.degree. C. and subjected to blow molding under a
blow pressure of about 7.times.10.sup.5 Pa for one second and then
under a blow pressure of about 30.times.10.sup.5 Pa for 40 seconds
for heat setting, while stretching it in the height direction by a
stretching rod, followed by cooling in air to obtain 500 bottles
having an outer diameter of about 95 mm, a height of about 305 mm,
an average wall thickness of the body portion of about 0.37 mm, a
weight of about 60 g and an internal capacity of about 1.5 l. With
respect to the obtained 498th to 500th bottles, the aroma-retention
property was measured and evaluated by the following method, and
the results are shown in Table 1.
Aroma-Retention Property
[0069] In a bottle, a 100% orange juice was filled in a hot state,
tightly sealed with a cap and stored at 10.degree. C. for one
month, whereupon the cap was removed, and the aroma was subjected
to a sensory test by comparing it with a case where the orange
juice was stored under the same conditions in a glass bottle,
whereby evaluation was made under the following standards.
[0070] .largecircle.: there was no difference in aroma from the
glass bottle, and the aroma-retention property was good.
[0071] .DELTA.: the aroma was weak as compared with the glass
bottle, and the aroma-retention property was slightly poor.
[0072] X: the aroma was extremely weak as compared with the glass
bottle, and the aroma-retention property was inferior.
[0073] Further, with respect to the obtained 491st to 500th
bottles, the surface appearance of the body portion of each bottle
was visually observed and evaluated under the following standards,
to evaluate the mold contamination, and the results are shown in
Table 1.
[0074] .circleincircle.: the surface was smooth, and no mold
contamination was observed.
[0075] .largecircle.: the surface smoothness was slightly inferior,
and accordingly, the mold contamination was slightly observed but
was not practically problematic.
[0076] X: the surface was roughened, deposition of foreign matters
was observed, and the mold contamination was substantial.
EXAMPLES 2 TO 6
[0077] The operation was carried out in the same manner as in
Example 1 except that the amounts of ethyl acid phosphate,
magnesium acetate and tetra-n-butoxy titanium at the time of the
melt polycondensation were changed as shown in Table 1, and then
results are shown in Table 1.
EXAMPLE 7
[0078] The operation was carried out in the same manner as in
Example 2 except that the solid phase polycondensation polyester
resin obtained in Example 2 was further subjected to water
treatment by immersing it in hot water of 90.degree. C. for two
hours, and the results are shown in Table 1.
EXAMPLE 8
[0079] The operation was carried out in the same manner as in
Example 7 except that the polyester resin obtained in Example 7 was
used, and a low density polyethylene was added at the time of the
injection molding of the stepped molding plate and at the time of
the injection molding of the preform, and the results are shown in
Table 1.
COMPARATIVE EXAMPLE 1
[0080] The operation was carried out in the same manner as in
Example 1 except that at the time of the melt polycondensation,
ethyl acid phosphate, magnesium acetate and antimony trioxide were
sequentially added in their ethylene glycol solutions,
respectively, with intervals of 5 minutes, and the respective
amounts were adjusted as shown in Table 1, and the results are
shown in Table 1.
COMPARATIVE EXAMPLE 2
[0081] The operation was carried out in the same manner as in
Example 1 except that at the time of the melt polycondensation,
orthophosphoric acid and germanium dioxide were sequentially added
in their ethylene glycol solutions, respectively, with intervals of
5 minutes, and the respective amounts were adjusted as shown in
Table 1, and the results are shown in Table 1.
COMPARATIVE EXAMPLE 3
[0082] The operation was carried out in the same manner as in
Comparative Example 2 except that the amount of germanium dioxide
was changed, and the obtained solid phase polycondensation
polyester resin was further subjected to water treatment by dipping
it in hot water at 90.degree. C. for 4 hours, and the results are
shown in Table 1.
COMPARATIVE EXAMPLE 4
[0083] The operation was carried out in the same manner as in
Example 1 except that at the time of the melt polycondensation,
tetra-n-butoxy titanium, magnesium acetate and ethyl acid phosphate
were sequentially added in their ethylene glycol solutions,
respectively, with intervals of 5 minutes, and the respective
amounts were adjusted as shown in Table 1, and the results are
shown in Table 1. TABLE-US-00001 TABLE 1 Examples 1 2 3 4 5 6 7 8
Copolymerizable Diethylene glycol 1.8 1.7 1.8 1.6 1.6 1.7 1.7 1.7
components (mol % based on diol) Contents of Titanium atoms (T)
(mol/t) 0.063 0.063 0.063 0.063 0.063 0.125 0.063 0.063 metal atoms
Magnesium atoms (M) (mol/t) 0.062 0.123 0.247 0.123 0.123 0.247
0.123 0.123 Germanium atoms (Ge) (mol/t) Antimony atoms (Sb)
(mol/t) Phosphorus atoms (P) (mol/t) 0.387 0.387 0.387 0.194 0.065
0.387 0.387 0.387 P/T (mol/mol) 6.14 6.14 6.14 3.08 1.03 3.10 6.14
6.14 M/T (mol/mol) 0.98 1.95 3.92 1.95 1.95 1.98 1.95 1.95 P/M
(mol/mol) 6.24 3.15 1.57 1.58 0.53 1.57 3.15 3.15 P/(T + M)
(mol/mol) 3.10 2.08 1.25 1.04 0.35 1.04 2.08 2.08 Resin chips
Intrinsic viscosity [.eta.] (dl/g) 0.74 0.75 0.75 0.73 0.74 0.74
0.75 0.75 Color coordinate b +2.6 +1.8 +2.4 +2.4 +3.4 +4.7 +1.8
+1.8 Cyclic trimer (wt %) 0.29 0.32 0.33 0.29 0.27 0.22 0.32 0.32
content (CT) Stepped molded Absorbance 395 nm 0.16 0.11 0.15 0.14
0.19 0.26 0.11 0.11 plate 500 nm 0.02 0.02 0.02 0.02 0.02 0.02 0.02
0.02 Temperature-rising (.degree. C.) 165 166 165 172 178 165 164
161 crystallization temperature (Tc) Bottle Aroma-retention
property .largecircle. .largecircle. .largecircle. .largecircle.
.largecircle. .largecircle. .largecircle. .largecircle. Mold
contamination property .largecircle. .largecircle. .largecircle.
.largecircle. .largecircle. .largecircle. .circleincircle.
.circleincircle. Comparative Example 1 2 3 4 Copolymerizable
Diethylene glycol 3.5 2.5 2.5 3.8 components (mol % based on diol)
Contents of Titanium atoms (T) (mol/t) 1.086 metal atoms Magnesium
atoms (Mg) (mol/t) 2.057 2.180 Germanium atoms (Ge) (mol/t) 0.551
0.716 Antimony atoms (Sb) (mol/t) 1.372 Phosphorus atoms (P)
(mol/t) 2.906 0.969 0.969 0.549 P/T (mol/mol) -- -- -- 0.5 M/T
(mol/mol) -- -- -- 2.00 P/M (mol/mol) 1.41 -- -- 0.25 P/(T + M)
(mol/mol) -- -- -- 0.17 Resin chips Intrinsic viscosity [.eta.]
(dl/g) 0.78 0.76 0.76 0.75 Color coordinate b +0.8 +0.9 +1.2 +14.3
Cyclic trimer content (CT) (wt %) 0.40 0.42 0.32 0.34 Stepped
molded Absorbance 395 nm 0.04 0.06 0.05 0.42 plate 500 nm 0.01 0.01
0.01 0.06 Temperature-rising (.degree. C.) 142 168 166 153
crystallization temperature (Tc) Bottle Aroma-retention property X
.DELTA. .DELTA. X Mold contamination property .largecircle.
.largecircle. .circleincircle. X
EXAMPLE 9
[0084] Using a continuous polymerization apparatus comprising a
slurry preparation tank, esterification reactors of two stages
connected in series thereto and melt polycondensation tanks of
three stages connected in series to the second stage esterification
reactor, terephthalic acid and ethylene glycol were continuously
supplied in a weight ratio of 865:485 to the slurry preparation
tank, and a 0.3 wt % ethylene glycol solution of ethyl acid
phosphate, was continuously added in such an amount that the
content as phosphorus atoms (P) per 1 ton of the formed polyester
resin would be 0.194 mol, followed by stirring and mixing to obtain
a slurry. This slurry was transferred to the first stage
esterification reactor set for an average retention time of 4 hours
in a nitrogen atmosphere at 260.degree. C. under a relative
pressure of 50 kPa (0.5 kg/cm.sup.2G) and then to the second stage
esterification reactor set for an average retention time of 1.5
hours in a nitrogen atmosphere at 260.degree. C. under a relative
pressure of 5 kPa (0.05 kg/cm.sup.2G), to carry out the
esterification reaction. At that time, the average esterification
ratio as measured by the following method, was 85% in the first
stage and 95% in the second stage.
Average Esterification Ratio
[0085] With respect to a solution having a sample dissolved at a
concentration of 3 wt % in a mixed solvent of deuterated
chloroform/hexafluoroisopropanol (weight ratio: 7/3), .sup.1H-NMR
was measured by a nuclear magnetic resonance apparatus ("JNM-EX270
model", manufactured by Nihon Denshi K.K.), and each peak was
identified. The amount of terminal carboxyl groups (A mol/ton
sample) was calculated from the integral value of the peak, and by
the following formula, the esterification ratio (E %) was
calculated as a proportion of the esterified among all carboxyl
groups of terephthalic acid units. Esterification
ratio(E)=[1-A/{(1,000,000/192.2).times.2}].times.100
[0086] Further, at that time, via an upper pipe provided at the
second stage, a 0.6 wt % ethylene glycol solution of magnesium
acetate tetrahydrate was continuously added in such an amount that
the content as magnesium atoms (Mg) per 1 ton of the formed
polyester resin would be 0.247 mol.
[0087] Continuously, at the time of transporting the esterification
reaction product obtained as described above to the melt
polycondensation tank, tetrabutyl titanate in the form of an
ethylene glycol solution having a concentration of titanium atoms
of 0.15 wt % and a water concentration of 0.5 wt %, was
continuously added to the esterification reaction product in the
transportation pipe in such an amount that the content as titanium
atoms (Ti) per 1 ton of the formed polyester resin would be 0.063
mol, and the esterification reaction product was continuously
transferred to the first stage melt polycondensation tank set at
270.degree. C. under an absolute pressure of 2.6 kPa (20 Torr),
then to the second stage melt polycondensation tank set at
278.degree. C. under an absolute pressure of 0.5 kPa (4 Torr) and
then to the third stage melt polycondensation tank set at
280.degree. C. under an absolute pressure of 0.3 kPa (2 Torr), to
carry out the melt polycondensation for a total of 3.17 hours by
adjusting the retention times in the respective polycondensation
tanks so that the intrinsic viscosity ([.eta..sub.1]) of the
obtained polyester resin would be 0.56 dl/g, whereupon the product
is withdrawn in the form of a strand from a discharge outlet
provided at the bottom of the polycondensation tank, cooled with
water and then cut by a cutter to obtain a polyester resin in the
form of chips.
[0088] Then, the polyester resin chips obtained as described above
were continuously supplied for crystallization to an agitation
crystallization machine held at about 160.degree. C. in a nitrogen
atmosphere so that the retention time would be about 60 minutes and
then continuously supplied to a tower type solid polycondensation
apparatus and heated at 205.degree. C. in a nitrogen atmosphere for
19 hours for solid phase polycondensation by adjusting the
retention time so that the intrinsic viscosity ([.eta..sub.2]) of
the obtained polyester resin would be 0.75 dl/g. The intrinsic
viscosity ([.eta..sub.1]) of the above melt polycondensate resin
and the intrinsic viscosity ([.eta..sub.2]) of the solid
polycondensate resin, were measured by the above-mentioned
method.
[0089] Further, the melt polycondensation rate (V.sub.1) as a value
obtained by dividing the intrinsic viscosity ([.eta..sub.1]) of the
above melt polycondensate resin by the melt polycondensation time,
the solid phase polycondensation rate (V.sub.2) as a value obtained
by dividing the difference ([.eta..sub.2]-[.eta..sub.1]) between
the above intrinsic viscosity ([.eta..sub.2]) of the above solid
polycondensate resin and the intrinsic viscosity ([.eta..sub.1]) of
the above melt polycondensate resin, by the solid phase
polycondensation time, and the ratio (V.sub.2/V.sub.1) of the solid
phase polycondensation rate (V.sub.2) to the melt polycondensation
rate (V.sub.1), were calculated, respectively, and the results are
shown in Table 2.
[0090] Further, with respect to the obtained solid phase
polycondensate resin chips, the contents of titanium atoms (Ti),
magnesium atoms (Mg) and phosphorus atoms (P) of the titanium
component, the magnesium component and the phosphorus component,
respectively, per 1 ton of the resin, were measured by the
above-mentioned methods, and the results are shown in Table 2.
[0091] Further, with respect to the obtained solid phase
polycondensate resin chips, the copolymerized amount of diethylene
glycol, the cyclic trimer content (CT) and the color coordinate
value b as the color tone, were measured by the above-mentioned
methods, and the acetaldehyde content (AA.sub.1) was measured by
the following method. The results are shown in Table 2.
Acetaldehyde Content (AA.sub.1)
[0092] 5.0 g of a resin sample was accurately weighed and sealed in
together with 10 ml of pure water in a micro bomb having an
internal capacity of 50 ml under sealing with nitrogen, whereupon
heat extraction was carried out at 160.degree. C. for 2 hours. The
amount of acetaldehyde in the extracted solution was quantitatively
analyzed by gas chromatography ("GC-14A", manufactured by Shimadzu
Corporation) using isobutyl alcohol as the internal standard.
[0093] Then, the obtained resin was dried at 160.degree. C. for 4
hours in a nitrogen stream of 40 l/min in an inert oven ("IPHH-201
model", manufactured by ESPEC COMPANY), and then, by an injection
molding machine ("M-70AII-DM", manufactured by Meiki Co., Ltd.), a
stepped molded plate having a shape shown in FIG. 1, was
injection-molded at a cylinder temperature of 280.degree. C. under
a back pressure of 5.times.10.sup.5 Pa at an injection rate of 40
cc/sec under a dwell pressure of 35.times.10.sup.5 Pa at a mold
temperature of 25.degree. C. with a molding cycle of about 75
seconds.
[0094] With respect to the molded plate, the absorbances at
wavelengths of 395 nm and 500 nm were measured by the
above-mentioned method, and further, the acetaldehyde content
(AA.sub.2) and the haze, were measured by the following methods.
The results are shown in Table 2.
Acetaldehyde Content (AA.sub.2)
[0095] Using samples cut out in the form of chips of about
4.times.4 mm from the rear end portion having a thickness of 3.5 mm
(portion B in FIG. 1) in the molded plate, the measurement was
carried out by the same method as described above.
Haze
[0096] With respect to the portion having a thickness of 5.0 mm
(portion C in FIG. 1) in the molded plate, the haze was measured by
means of a haze meter ("NDH-300A", manufactured by NIPPON DENSHOKU
INDUSTRIES CO., LTD.).
[0097] Separately, the obtained polyester resin chips were dried at
130.degree. C. for 10 hours in a vacuum dryer. Then, by an
injection molding machine ("FE-80S", manufactured by Nissei Plastic
Industrial Co., Ltd.), a preform of a test tube shape having an
outer diameter of 29.0 mm, a height of 165 mm, an average wall
thickness of 3.7 mm and a weight of about 60 g, was
injection-molded at a cylinder temperature of 280.degree. C. under
a back pressure of 5.times.10.sup.5 Pa at an injection rate of 45
cc/sec under a dwell pressure of 30.times.10.sup.5 Pa at a mold
temperature of 20.degree. C. with a molding cycle of about 40
seconds.
[0098] The obtained preform was heated for 70 seconds in a near
infrared ray irradiation furnace equipped with a quartz heater and
then left to stand at room temperature for 25 seconds. Then, it was
introduced into a blow mold set at 130.degree. C. and blow-molded
under a blow pressure of 7.times.10.sup.5 Pa for one second and
further under a blow pressure of 30.times.10.sup.5 Pa for 5
seconds, while stretching in the height direction by an stretching
rod, heat-set and cooled in air to mold a bottle having an outer
diameter of about 95 mm, a height of about 305 mm, an average wall
thickness of the body portion of about 0.35 mm, a weight of about
60 g and an internal capacity of about 1.5 l.
[0099] With respect to the obtained bottle, the aroma-retention
property and the mold contamination were measured and evaluated by
the above-mentioned methods, and further, the acetaldehyde odor was
evaluated by the following method. The results are shown in Table
2.
Acetaldehyde Odor of the Bottle
[0100] The bottle was heated in an oven at 50.degree. C. for one
hour, whereupon the acetaldehyde odor was examined by a sensory
test and evaluated by five stages ranging from 5 (acetaldehyde odor
very little) to 1 (acetaldehyde odor assails ones nostrils).
EXAMPLES 10 TO 23, AND COMPARATIVE EXAMPLES 5 to 7
[0101] Polyester resin chips were prepared in the same manner as in
Example 9 except that the copolymerizable component and its amount,
the amounts and order for addition of the phosphorus compound, the
magnesium compound and the titanium compound, the concentration of
titanium atoms and the water concentration in the ethylene glycol
solution of the titanium compound, and the melt polycondensation
time and the solid phase polycondensation time, were changed as
identified in Table 2, and evaluated in the same manner. The
results are shown in Table 2. In Comparative Example 5, phosphorous
acid instead of ethyl acid phosphate, cobalt acetate tetrahydrate
instead of magnesium acetate tetrahydrate and titanium potassium
oxalate instead of tetrabutyl titanate, were used and added in the
order of titanium potassium oxalate, then cobalt acetate
tetrahydrate and then phosphorous acid. In Comparative Example 7,
orthophosphoric acid was used instead of ethyl acid phosphate, and
the order of addition was tetrabutyl titanate, then magnesium
acetate tetrahydrate and then orthophosphoric acid. TABLE-US-00002
TABLE 2 Examples 9 10 11 12 13 14 15 16 17 Copolymerizable
Diethylene glycol 2.2 2.2 2.2 2.2 2.2 2.2 1.7 2.2 2.2 components
(mol % based on diol) Isophthalic acid (mol % based 1.8 on
dicarboxylic acid) Ethylene Concentration of titanium atoms (wt %)
0.15 0.15 0.15 0.15 0.15 0.15 0.15 0.40 0.15 glycol solution of
Water concentration (wt %) 0.5 0.5 0.5 0.5 0.5 0.5 0.5 1.5 0.03 the
titanium compound Contents of Titanium atoms (T) (mol/t) 0.063
0.063 0.063 0.063 0.063 0.125 0.063 0.063 0.063 metal atoms
Magnesium atoms (M) (mol/t) 0.247 0.123 0.370 0.247 0.247 0.247
0.247 0.247 0.247 Cobalt atoms (M) (mol/t) Phosphorus atoms (P)
(mol/t) 0.194 0.194 0.194 0.065 0.387 0.387 0.194 0.194 0.194 P/T
(mol/mol) 3.1 3.1 3.1 1.0 6.2 3.1 3.1 3.1 3.1 M/T (mol/mol) 3.9 2.0
5.9 3.9 3.9 2.0 3.9 3.9 3.9 Polycondensation Melt polycondensation
time (hr) 3.17 3.33 3.00 3.00 3.33 3.00 3.17 3.25 3.25 rate
Intrinsic viscosity [.eta..sub.1] (dl/g) 0.56 0.56 0.56 0.56 0.56
0.56 0.56 0.56 0.56 Polycondensation rate (dl/g/hr) 0.177 0.168
0.187 0.187 0.168 0.187 0.177 0.172 0.172 (V.sub.1) Solid phase
polycondensation (hr) 19 20 22 18 28 18 18 20 20 time Intrinsic
viscosity [.eta..sub.2] (dl/g) 0.75 0.75 0.75 0.77 0.77 0.76 0.75
0.75 0.75 Polycondensation rate (V.sub.2) (dl/g/hr) 0.010 0.010
0.009 0.012 0.008 0.011 0.011 0.010 0.010 V.sub.2/V.sub.1 0.057
0.060 0.046 0.063 0.045 0.060 0.060 0.055 0.055 Resin chips
Acetaldehyde content (AA.sub.1) (ppm) 3 4 4 3 4 4 3 4 4 Cyclic
trimer content (CT) (wt %) 0.28 0.28 0.32 0.24 0.24 0.19 0.27 0.28
0.28 Color coordinate b +2.2 +2.4 +2.2 +3.4 +2.4 +4.7 +2.2 +2.4
+2.4 Stepped Absorbance 395 nm 0.16 0.14 0.16 0.20 0.15 0.26 0.16
0.16 0.16 molded plate 500 nm 0.02 0.02 0.02 0.02 0.02 0.02 0.02
0.02 0.02 Acetaldehyde content (AA.sub.2) (ppm) 16 18 15 20 14 20
14 16 16 Haze (%) 7 8 8 8 7 8 4 12 15 Bottle Aroma-retention
property .largecircle. .largecircle. .largecircle. .largecircle.
.largecircle. .largecircle. .largecircle. .largecircle.
.largecircle. Mold contamination property .largecircle.
.largecircle. .largecircle. .largecircle. .largecircle.
.largecircle. .largecircle. .largecircle. .largecircle.
Acetaldehyde odor 4 4 4 4 5 4 5 4 4 Comparative Examples Examples
18 19 20 21 22 23 5 6 7 Copolymerizable Diethylene glycol 2.2 2.2
2.2 2.2 2.2 2.2 3.1 2.8 3.8 components (mol % based on diol)
Isophthalic acid (mol % based on dicarboxylic acid) Ethylene
Concentration of titanium atoms (wt %) 0.15 0.15 0.15 0.15 0.15
0.15 0.15 0.15 0.15 glycol Water concentration (wt %) 0.5 0.5 0.5
0.5 0.5 0.5 0.03 0.03 0.03 solution of the titanium compound
Contents of Titanium atoms (T) (mol/t) 0.010 0.313 0.063 0.063
0.063 0.063 0.125 0.021 1.086 metal atoms Magnesium atoms (Mg)
(mol/t) 0.247 0.247 0.740 0.247 0.247 1.550 2.180 Cobalt atoms (M)
(mol/t) 1.033 Phosphorus atoms (P) (mol/t) 0.387 0.387 0.194 0.194
0.775 0.494 1.070 0.549 P/T (mol/mol) 37.1 1.2 3.1 3.1 0 12.4 3.9
51.2 0.5 M/T (mol/mol) 23.6 0.8 0 11.7 3.9 3.9 8.3 74.2 2.0
Polycondensation Melt polycondensation time (hr) 4.00 2.00 3.67
2.75 2.83 4.00 3.50 3.50 2.00 rate Intrinsic viscosity
[.eta..sub.1] (dl/g) 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56
Polycondensation rate (V.sub.1) (dl/g/hr) 0.140 0.280 0.153 0.204
0.198 0.140 0.160 0.160 0.280 Solid phase polycondensation (hr) 38
12 26 32 15 42 43 42 12 time Intrinsic viscosity [.eta..sub.2]
(dl/g) 0.76 0.76 0.75 0.75 0.77 0.77 0.75 0.75 0.75
Polycondensation rate (V.sub.2) (dl/g/hr) 0.005 0.017 0.007 0.006
0.014 0.005 0.004 0.005 0.016 V.sub.2/V.sub.1 0.038 0.060 0.048
0.029 0.071 0.036 0.028 0.029 0.057 Resin chips Acetaldehyde
content (AA.sub.1) (ppm) 4 11 4 4 3 4 8 3 11 Cyclic trimer content
(CT) (wt %) 0.55 0.17 0.28 0.56 0.21 0.45 0.88 0.49 0.34 Color
coordinate b +0.6 +11.3 +2.4 +2.4 +4.2 +2.4 -2.3 +2.2 +14.3 Stepped
Absorbance 395 nm 0.09 0.31 0.20 0.21 0.27 0.10 0.06 0.06 0.42
molded plate 500 nm 0.01 0.05 0.03 0.03 0.04 0.02 0.01 0.01 0.06
Acetaldehyde content (AA.sub.2) (ppm) 18 30 21 14 28 13 27 23 35
Haze (%) 7 12 9 8 12 7 8 8 70 Bottle Aroma-retention property
.largecircle. .largecircle. .largecircle. .largecircle.
.largecircle. .largecircle. X .largecircle. X Mold contamination
property .largecircle. .largecircle. .largecircle. .largecircle.
.largecircle. .largecircle. X .largecircle. X Acetaldehyde odor 4 1
3 5 2 5 2 3 1
INDUSTRIAL APPLICABILITY
[0102] According to the present invention, it is possible to
provide a polyester resin, whereby a molded product excellent in a
gas barrier property and also excellent in an ultraviolet shielding
property, color tone, etc., and which is particularly suitable for
molding a bottle for e.g. a beverage required to have an
aroma-retention property and further to provide a polyester resin,
whereby the acetaldehyde content in a molded product is reduced to
eliminate an influence over the taste, aroma, etc. of the content,
and a process for its production, whereby the polycondensability is
improved.
* * * * *