Thermo-shrinkable polyester film
Disclosed is a thermo-shrinkable polyester film in which shrinkage uniformity is ensured in a shrinking process thus realizing superior quality of the outer appearance without causing a poorly printed state, reducing the production cost of the shrinking process and improving the productivity.
1. A thermo-shrinkable polyester film having a rate of change of shrinkage ratio of 4.0-10.0%/sec in a main shrinking direction with respect to time within 5 sec at 95° C. upon measurement of thermal shrinkage-force in a predetermined longitudinal direction using a thermal stress tester.
2. The thermo-shrinkable polyester film according to claim 1 , which has the shrinkage stress of 0.6-1.3 kg/mm 2 in a main shrinking direction at 95° C.
3. The thermo-shrinkable polyester film according to claim 1 , wherein the velocity of shrinkage in a transverse direction as a main shrinking direction as represented by Equation 1 below is 0.5-3.5%/° C.:
Velocity of Shrinkage=Δ L/ΔT Equation 1
wherein the equation is obtained by measuring dimension changes of a sample due to expansion and shrinkage depending on changes in temperature using a linear variable differential transformer, in which ΔT is a change in temperature and ΔL is a deformation percentage in a transverse direction as a main shrinking direction, in a temperature range of 70-85° C.
4. The thermo-shrinkable polyester film according to claim 1 , which has a maximum shrinkage temperature of 85-100° C. in a main shrinking direction and a maximum shrinkage stress of 0.65-1.30 kg/mm 2 in a main shrinking direction, in which the maximum shrinkage temperature is defined as, on the graph of shrinkage stress versus temperature obtained by measuring stress of a film which is held under conditions of room temperature and a predetermined initial load (0.125 kg/mm 2 and is shrunk due to application of heat thereto at a predetermined heating rate (2.5° C./sec), a first temperature showing the maximum shrinkage stress, and the maximum shrinkage stress is defined as a peak of the graph of shrinkage stress versus temperature obtained by measuring stress of a film which is held under conditions of room temperature and a predetermined initial load (0.125 kg/mm 2 ) and is shrunk due to application of heat thereto at a predetermined heating rate (2.5° C./sec).
5. The thermo-shrinkable polyester film according to claim 1 , which has a dynamic glass transition temperature of 90-100° C. in a main shrinking direction as measured through dynamic mechanical thermal analysis and an intrinsic viscosity of 0.60-0.70 dl/g.
6. The thermo-shrinkable polyester film according to claim 1 , which has a rate of shrinkage deformation of 3.5-8.5 in a transverse direction as a main shrinking direction as represented by Equation 2 below:
Rate of Shrinkage Deformation= dL/dT Equation 2
wherein the value is obtained by differentiating the deformation percentage in a transverse direction as a main shrinking direction depending on the change in temperature in a temperature range of 30-90° C. as represented by Equation 1 showing dimension changes of a sample due to expansion and shrinkage depending on changes in temperature measured using a linear variable differential transformer, and indicates a maximum rate of deformation in the temperature range.
7. The thermo-shrinkable polyester film according to claim 1 , which has a thermal shrinkage ratio of 60% or more (at 95° C., 10 sec, free state) in a transverse direction as a main shrinking direction.
8. The thermo-shrinkable polyester film according to claim 1 , which comprises at least one copolyester prepared from one or more dicarboxylic acid and two or more diols, or a mixture of a homopolyester and the copolyester,
wherein said dicarboxylic acid is selected from the group consisting of terephthalic acid, oxalic acid, malonic acid, succinic acid, adipic acid, suberic acid, azelaic acid, sebacic acid, phthalic acid, isophthalic acid, naphthalene dicarboxylic acid and diphenylether dicarboxylic acid, and
said diols are selected from the group consisting of ethyleneglycol, neopentylglycol, propyleneglycol, trimethyleneglycol, tetramethyleneglycol, hexamethyleneglycol, diethyleneglycol, polyalkyleneglycol and 1,4-cyclohexanedimethanol.
9. The thermo-shrinkable polyester film according to claim 1 , which is manufactured by subjecting the polyester to extrusion at 200-350° C., preheating at 80-100° C. and then stretching in a transverse direction at 70-95° C.
10. The thermo-shrinkable polyester film according to claim 1 , which is manufactured by subjecting the polyester to extrusion, preheating, stretching in a transverse direction and then heat treatment, wherein a temperature for the heat treatment is set to be lower than a temperature for the preheating.
11. A thermo-shrinkable polyester film having a shrinkage starting temperature of 72-88° C. in a main shrinking direction, in which the shrinkage starting temperature is defined as, on a graph of shrinkage stress versus temperature obtained by measuring stress of a film which is held under conditions of room temperature and a predetermined initial load (0.125 Kg/mm 2 ) and is shrunk due to application of heat thereto at a predetermined heating rate (2.5° C./sec), a first temperature showing shrinkage stress having a value equal to the initial load, wherein the velocity of shrinkage in a transverse direction as a main shrinking direction as represented by Equation 1 below is 0.5-3.5%/° C.:
Velocity of Shrinkage=Δ L/ΔT Equation 1
wherein the equation is obtained by measuring dimension changes of a sample due to expansion and shrinkage depending on changes in temperature using a linear variable differential transformer, in which ΔT is a change in temperature and ΔL is a deformation percentage in a transverse direction as a main shrinking direction, in a temperature range of 70-85° C.
12. A thermo-shrinkable polyester film having a shrinkage starting temperature of 72-88° C. in a main shrinking direction, in which the shrinkage starting temperature is defined as, on a graph of shrinkage stress versus temperature obtained by measuring stress of a film which is held under conditions of room temperature and a predetermined initial load (0.125 Kg/mm 2 ) and is shrunk due to application of heat thereto at a predetermined heating rate (2.5° C./sec), a first temperature showing shrinkage stress having a value equal to the initial load, wherein the rate of change of shrinkage ratio in a main shrinking direction with respect to time within 5 sec at 95° C. upon measurement of thermal shrinkage-force in a predetermined longitudinal direction using a thermal stress tester is 4.0-10.0%/sec.
13. The thermo-shrinkable polyester film according to claim 12 , which has the shrinkage stress of 0.6-1.3 kg/mm 2 in a main shrinking direction at 95° C.
14. A thermo-shrinkable polyester film having a shrinkage starting temperature of 72-88° C. in a main shrinking direction, in which the shrinkage starting temperature is defined as, on a graph of shrinkage stress versus temperature obtained by measuring stress of a film which is held under conditions of room temperature and a predetermined initial load (0.125 Kg/mm 2 ) and is shrunk due to application of heat thereto at a predetermined heating rate (2.5° C./sec), a first temperature showing shrinkage stress having a value equal to the initial load, wherein the thermo-shrinkable polyester film has a maximum shrinkage temperature of 85-100° C. in a main shrinking direction and a maximum shrinkage stress of 0.65-1.30 kg/mm 2 in a main shrinking direction, in which the maximum shrinkage temperature is defined as, on the graph of shrinkage stress versus temperature obtained by measuring stress of a film which is held under conditions of room temperature and a predetermined initial load (0.125 kg/mm 2 ) and is shrunk due to application of heat thereto at a predetermined heating rate (2.5° C./sec), a first temperature showing the maximum shrinkage stress, and the maximum shrinkage stress is defined as a peak of the graph of shrinkage stress versus temperature obtained by measuring stress of a film which is held under conditions of room temperature and a predetermined initial load (0.125 kg/mm 2 ) and is shrunk due to application of heat thereto at a predetermined heating rate (2.5° C./sec).
15. A thermo-shrinkable polyester film having a shrinkage starting temperature of 72-88° C. in a main shrinking direction, in which the shrinkage starting temperature is defined as, on a graph of shrinkage stress versus temperature obtained by measuring stress of a film which is held under conditions of room temperature and a predetermined initial load (0.125 Kg/mm 2 ) and is shrunk due to application of heat thereto at a predetermined heating rate (2.5° C./sec), a first temperature showing shrinkage stress having a value equal to the initial load, wherein the thermo-shrinkable polyester film has a dynamic glass transition temperature of 90-100° C. in a main shrinking direction as measured through dynamic mechanical thermal analysis and an intrinsic viscosity of 0.60-0.70 dl/g.
16. A thermo-shrinkable polyester film having a shrinkage starting temperature of 72-88° C. in a main shrinking direction, in which the shrinkage starting temperature is defined as, on a graph of shrinkage stress versus temperature obtained by measuring stress of a film which is held under conditions of room temperature and a predetermined initial load (0.125 Kg/mm 2 ) and is shrunk due to application of heat thereto at a predetermined heating rate (2.5° C./sec), a first temperature showing shrinkage stress having a value equal to the initial load, wherein the thermo-shrinkable polyester film has a rate of shrinkage deformation of 3.5-8.5 in a transverse direction as a main shrinking direction as represented by Equation 2 below:
Rate of Shrinkage Deformation= dL/dT Equation 2
wherein the value is obtained by differentiating the deformation percentage in a transverse direction as a main shrinking direction depending on the change in temperature in a temperature range of 30-90° C. as represented by Equation 1 showing dimension changes of a sample due to expansion and shrinkage depending on changes in temperature measured using a linear variable differential transformer, and indicates a maximum rate of deformation in the temperature range.
17. The thermo-shrinkable polyester film according to claim 16 , wherein a temperature range in which the maximum rate of shrinkage deformation in a transverse direction as a main shrinking direction is exhibited is 80-88° C.
18. A thermo-shrinkable polyester film having a shrinkage starting temperature of 72-88° C. in a main shrinking direction, in which the shrinkage starting temperature is defined as, on a graph of shrinkage stress versus temperature obtained by measuring stress of a film which is held under conditions of room temperature and a predetermined initial load (0.125 Kg/mm 2 ) and is shrunk due to application of heat thereto at a predetermined heating rate (2.5° C./sec), a first temperature showing shrinkage stress having a value equal to the initial load, wherein the thermo-shrinkable polyester film has a thermal shrinkage ratio of 60% or more (at 95° C., 10 sec, free state) in a transverse direction as a main shrinking direction.
19. A thermo-shrinkable polyester film having a shrinkage starting temperature of 72-88° C. in a main shrinking direction, in which the shrinkage starting temperature is defined as, on a graph of shrinkage stress versus temperature obtained by measuring stress of a film which is held under conditions of room temperature and a predetermined initial load (0.125 Kg/mm 2 ) and is shrunk due to application of heat thereto at a predetermined heating rate (2.5° C./sec), a first temperature showing shrinkage stress having a value equal to the initial load,
wherein the thermo-shrinkable polyester film comprises at least one copolyester prepared from one or more dicarboxylic acid and two or more diols, or a mixture of a homopolyester and the copolyester,
wherein said dicarboxylic acid is selected from the group consisting of terephthalic acid, oxalic acid, malonic acid, succinic acid, adipic acid, suberic acid, azelaic acid, sebacic acid, phthalic acid, isophthalic acid, naphthalene dicarboxylic acid and diphenylether dicarboxylic acid; and said diols comprise ethyleneglycol and another diol selected from the group consisting of neopentylglycol, propyleneglycol, trimethyleneglycol, tetramethyleneglycol, hexamethyleneglycol, diethyleneglycol, polyalkyleneglycol and 1,4-cyclohexanedimethanol,
wherein the the dicarboxylic acid includes about 80 mol % or more of a terephthalic acid and wherein the content of the another diol is about 14-24 mol % based on the total amount of the diols.
20. The thermo-shrinkable polyester film according to claim 19 , wherein the copolyester has a glass transition temperature of 67-77° C. and an intrinsic viscosity of 0.60-0.70 dl/g.
21. A thermo-shrinkable polyester film having a shrinkage starting temperature of 72-88° C. in a main shrinking direction, in which the shrinkage starting temperature is defined as, on a graph of shrinkage stress versus temperature obtained by measuring stress of a film which is held under conditions of room temperature and a predetermined initial load (0.125 Kg/mm 2 ) and is shrunk due to application of heat thereto at a predetermined heating rate (2.5° C./sec), a first temperature showing shrinkage stress having a value equal to the initial load,
wherein the thermo-shrinkable polyester film comprises at least one copolyester prepared from one or more dicarboxylic acid and two or more diols, or a mixture of a homopolyester and the copolyester, and
wherein the homopolyester comprises polybutyleneterephthalate or polytriethyleneterephthalate.
22. A thermo-shrinkable polyester film having a shrinkage starting temperature of 72-88° C. in a main shrinking direction, in which the shrinkage starting temperature is defined as, on a graph of shrinkage stress versus temperature obtained by measuring stress of a film which is held under conditions of room temperature and a predetermined initial load (0.125 Kg/mm 2 ) and is shrunk due to application of heat thereto at a predetermined heating rate (2.5° C./sec), a first temperature showing shrinkage stress having a value equal to the initial load,
wherein the thermo-shrinkable polyester film comprises at least one copolyester prepared from one or more dicarboxylic acid and two or more diols, or a mixture of a homopolyester and the copolyester,
wherein said dicarboxylic acid is selected from the group consisting of terephthalic acid, oxalic acid, malonic acid, succinic acid, adipic acid, suberic acid, azelaic acid, sebacic acid, phthalic acid, isophthalic acid, naphthalene dicarboxylic acid and diphenylether dicarboxylic acid; and said diols are selected from the group consisting of ethyleneglycol, neopentylglycol, propyleneglycol, trimethyleneglycol, tetramethyleneglycol, hexamethyleneglycol, diethyleneglycol, polyalkyleneglycol and 1,4-cyclohexanedimethanol, and
wherein the copolyester is used in an amount of 85-93 wt % based on a total amount of the polyester.
23. A method of manufacturing a thermo-shrinkable polyester film through extrusion and stretching of polyester, comprising:
extruding polyester at 200-350° C., thus obtaining an extruded polyester sheet;
preheating the extruded polyester sheet at 80-100° C.; and
stretching the polyester sheet in a transverse direction at 70-95° C.,
wherein the thermo-shrinkable polyester film has a shrinkage starting temperature of 72-88° C. in a main shrinking direction, in which the shrinkage starting temperature is defined as, on a graph of shrinkage stress versus temperature obtained by measuring stress of a film which is held under conditions of room temperature and a predetermined initial load (0.125 Kg/mm 2 ) and is shrunk due to application of heat thereto at a predetermined heating rate (2.5° C./sec), a first temperature showing shrinkage stress having a value equal to the initial load.
24. A method of manufacturing a thermo-shrinkable polyester film through extrusion and stretching of polyester, comprising:
extruding polyester at 200-350° C., thus obtaining an extruded polyester sheet;
preheating the extruded polyester sheet;
stretching the polyester sheet; and
heat treating the polyester sheet, wherein a temperature for the heat treating is set to be lower than a temperature for the preheating, and the thermo-shrinkable polyester film has a rate of change of shrinking ratio of 4.0-10.0%/sec in a main shrinking direction with respect to time within 5 sec at 95° C. upon measurement of thermal shrinkage-force in a predetermined longitudinal direction using a thermal stress tester.
25. The method according to claim 24 , wherein the preheating is performed at 80-100° C., and the heat treating is performed in a temperature range of from room temperature to 95° C.
26. A thermo-shrinkable polyester film having a velocity of shrinkage of 0.5-3.5%/° C. in a transverse direction as a main shrinking direction, as represented by Equation 1 below:
Velocity of Shrinkage=Δ L/ΔT Equation 1
wherein the equation is obtained by measuring dimension changes of a sample due to expansion and shrinkage depending on changes in temperature using a linear variable differential transformer, in which ΔT is a change in temperature and ΔL is a deformation percentage in a transverse direction as a main shrinking direction, in a temperature range of 70-85° C.,
wherein the rate of change of shrinkage ratio in a main shrinking direction with respect to time within 5 sec at 95° C. upon measurement of thermal shrinkage-force in a predetermined longitudinal direction using a thermal stress tester is 4.0-10.0%/sec.
27. A thermo-shrinkable polyester film having a velocity of shrinkage of 0.5-3.5%/° C. in a transverse direction as a main shrinking direction, as represented by Equation 1 below:
Velocity of Shrinkage= ΔL/ΔT Equation 1
wherein the equation is obtained by measuring dimension changes of a sample due to expansion and shrinkage depending on changes in temperature using a linear variable differential transformer, in which ΔT is a change in temperature and ΔL is a deformation percentage in a transverse direction as a main shrinking direction, in a temperature range of 70-85° C.,
wherein the thermo-shrinkable polyester film has a maximum shrinkage temperature of 85-100° C. in a main shrinking direction and a maximum shrinkage stress of 0.65-1.30 kg/mm 2 in a main shrinking direction, in which the maximum shrinkage temperature is defined as, on the graph of shrinkage stress versus temperature obtained by measuring stress of a film which is held under conditions of room temperature and a predetermined initial load (0.125 kg/mm 2 )and is shrunk due to application of heat thereto at a predetermined heating rate (2.5° C./sec), a first temperature showing the maximum shrinkage stress, and the maximum shrinkage stress is defined as a peak of the graph of shrinkage stress versus temperature obtained by measuring stress of a film which is held under conditions of room temperature and a predetermined initial load (0.125 kg/mm 2 ) and is shrunk due to application of heat thereto at a predetermined heating rate (2.5° C./sec).
28. A thermo-shrinkable polyester film having a velocity of shrinkage of 0.5-3.5%/° C. in a transverse direction as a main shrinking direction, as represented by Equation 1 below:
Velocity of Shrinkage= ΔL/ΔT Equation 1
wherein the equation is obtained by measuring dimension changes of a sample due to expansion and shrinkage depending on changes in temperature using a linear variable differential transformer, in which ΔT is a change in temperature and ΔL is a deformation percentage in a transverse direction as a main shrinking direction, in a temperature range of 70-85° C.,
wherein the thermo-shrinkable polyester film has a dynamic glass transition temperature of 90-100° C. in a main shrinking direction as measured through dynamic mechanical thermal analysis and an intrinsic viscosity of 0.60-0.70 dl/g.
29. A thermo-shrinkable polyester film having a velocity of shrinkage of 0.5-3.5%/° C. in a transverse direction as a main shrinking direction, as represented by Equation 1 below:
Velocity of Shrinkage= ΔL/ΔT Equation 1
wherein the equation is obtained by measuring dimension changes of a sample due to expansion and shrinkage depending on changes in temperature using a linear variable differential transformer, in which ΔT is a change in temperature and ΔL is a deformation percentage in a transverse direction as a main shrinking direction, in a temperature range of 70-85° C.,
wherein the thermo-shrinkable polyester film has a rate of shrinkage deformation of 3.5-8.5 in a transverse direction as a main shrinking direction as represented by Equation 2 below:
Rate of Shrinkage Deformation= dL/dT Equation 2
wherein the value is obtained by differentiating the deformation percentage in a transverse direction as a main shrinking direction depending on the change in temperature in a temperature range of 30-90° C. as represented by Equation 1 showing dimension changes of a sample due to expansion and shrinkage depending on changes in temperature measured using a linear variable differential transformer, and indicates a maximum rate of deformation in the temperature range.
30. A thermo-shrinkable polyester film having a velocity of shrinkage of 0.5-3.5%/° C. in a transverse direction as a main shrinking direction, as represented by Equation 1 below:
Velocity of Shrinkage= ΔL/ΔT Equation 1
wherein the equation is obtained by measuring dimension changes of a sample due to expansion and shrinkage depending on changes in temperature using a linear variable differential transformer, in which ΔT is a change in temperature and ΔL is a deformation percentage in a transverse direction as a main shrinking direction, in a temperature range of 70-85° C.,
wherein the thermo-shrinkable polyester film has a thermal shrinkage ratio of 60% or more (at 95° C., 10 sec, free state) in a transverse direction as a main shrinking direction.