AU2019226120B2

AU2019226120B2 - Polyester film and method for reproducing polyester container using same

Info

Publication number: AU2019226120B2
Application number: AU2019226120A
Authority: AU
Inventors: Eugene Jung; Chul Kyu Kim; Yong Deuk Kim; Jung Kyu Lee; Dae Yong Shin; Jaehyong Son; Joo Ho Yang
Original assignee: SK Microworks Co Ltd; Microworks America Inc
Current assignee: Microworks Co Ltd; Microworks America Inc
Priority date: 2018-04-30
Filing date: 2019-04-30
Publication date: 2020-07-09
Anticipated expiration: 2039-04-30
Also published as: AU2019226120A1

Abstract

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Description

Title of Invention

POLYESTER FILM AND METHOD FOR REPRODUCING POLYESTER CONTAINER USING SAME

Technical Field

Embodiments relate to a polyester film and a process for regenerating a polyester

container using the same, which not only solve the environmental problems by

improving the recyclability of the polyester container, but also are capable of

enhancing the yield and productivity.

Background Art

As concerns about environmental problems have increased in recent years, there is

a demand for addressing the recycling issues of products fabricated using thermoplastic

polymers. In particular, polyethylene terephthalate, a thermoplastic resin having

excellent properties in terms of thermal resistivity, processability, transparency, and

non-toxicity, has been widely used for producing a wide range of products such as films,

fibers, bottles, containers, and the like, and efforts have been made to improve the

regeneration rate thereof.

In general, a polyolefin stretch film or the like is attached to a container

produced from polyethylene terephthalate as a label. Thus, once a container recycled

from the consumers has been washed and crushed, it is then subjected to liquid specific

gravity separation, dehydration, drying, and/or wind specific gravity separation in order

to remove a large amount of films contained in the crushed product and then to such an

additional step as pelletization to obtain regenerated polyester chips. However, there

has been a disadvantage in that the films are not completely removed even after the

above steps; and that the regenerated polyester chips are colored due to the inks contained in the films, or they are non-uniformly clumped during the thermal treatment thereof. Accordingly, a method of using a film made of a low specific gravity polymer such as polystyrene, polyethylene, polypropylene, and the like as a label has been proposed in order to readily carry out the specific gravity separation. However, the low specific gravity thereof cannot be effectively achieved due to the ink layer, which makes it difficult to completely separate the films, and the problem that the residual ink colors the regenerated chips cannot be solved. Any discussion of documents, acts, materials, devices, articles or the like which has been included in the present specification is not to be taken as an admission that any or all of these matters form part of the prior art base or were common general knowledge in the field relevant to the present disclosure as it existed before the priority date of each of the appended claims. Throughout this specification the word "comprise", or variations such as "comprises" or "comprising", will be understood to imply the inclusion of a stated element, integer or step, or group of elements, integers or steps, but not the exclusion of any other element, integer or step, or group of elements, integers or steps.

Disclosure of Invention Technical Problem Accordingly, embodiments aim to provide a polyester film capable of preventing the clumping caused by residual ink during the regeneration process, thereby improving the recyclability of a polyester container, and a process for regenerating a polyester container using the same. Summary In one aspect of the disclosure there is provided a polyester film, which comprises a copolymerized polyester resin comprising a diol component and a dicarboxylic acid component and has a heat shrinkage rate of 30% or more in the main shrinkage direction upon thermal treatment at a temperature of 80°C for 10 seconds and a melting point of 170C or higher as measured by differential scanning calorimetry, wherein the crystallization temperature of the polyester film is not measured or is 70°C to 95°C by differential scanning calorimetry, wherein the heat of crystallization of the polyester film at the crystallization temperature is not measured or is 0.01 to 50 J/g, and wherein the copolymerized polyester resin comprises ethylene glycol in an amount of 55 to 94% by mole based on the total number of moles of the diol component.

Solution to Problem According to an embodiment, there is provided a polyester film, which comprises a copolymerized polyester resin comprising a diol component and a dicarboxylic acid component and has a heat shrinkage rate of 30% or more in the main shrinkage direction upon thermal treatment at a temperature of 80°C for 10 seconds and a melting point of 170C or higher as measured by differential scanning calorimetry. According to an embodiment, there is provided a polyester film, which comprises a copolymerized polyester resin comprising a diol component and a dicarboxylic acid component and has a haze of 50% or less when immersed in a 1% aqueous solution of NaOH for 15 minutes. According to an embodiment, there is provided a polyester film, which

2A comprises a first layer comprising a copolymerized polyester resin comprising a diol component and a dicarboxylic acid component and a second layer comprising a resin having a glass transition temperature (Tg) of 70°C or higher.

According to an embodiment, there is provided a process for regenerating a

polyester container, which comprises preparing the polyester container provided with

the polyester film; crushing the container provided with the polyester film to obtain

flakes; and thermally treating the flakes to produce regenerated polyester chips,

wherein when the flakes are thermally treated at a temperature of 2000 C to 2200 C for

60 minutes to 120 minutes, the clumping fraction is 8% or less, and the flakes comprise

first flakes obtained by crushing the container and second flakes obtained by crushing

the polyester film.

Advantageous Effects of Invention

The polyester film according to the embodiments improves the recyclability

of a polyester container, thereby solving the environmental problems, and enhances the

yield and productivity.

In addition, the process for regenerating a polyester container according to the

embodiment does not require a separate step of separating the polyester container and a

film, thereby saving time and cost.

Brief Description of Drawings

Fig. 1 schematically depicts a process for regenerating a polyester container

according to an embodiment.

Fig. 2 shows the heat shrinkage rates of the polyester films of Examples 1-1 to

1-4 and Comparative Example 1-1.

Best Mode for Carrying out the Invention

Hereinafter, the present invention will be described in detail with reference to embodiments. The embodiments are not limited to those described below. Rather, they can be modified into various forms as long as the gist of the invention is not altered.

Throughout the present specification, when a part is referred to as "comprising"

an element, it is understood that other elements may be comprised, rather than other

elements are excluded, unless specifically stated otherwise.

All numbers and expressions relating to quantities of components, reaction

conditions, and the like used herein are to be understood as being modified by the term

"about" unless specifically stated otherwise.

Polyester film

According to an embodiment, there is provided a polyester film, which

comprises a copolymerized polyester resin comprising a diol component and a

dicarboxylic acid component and has a heat shrinkage rate of 30% or more in the main

shrinkage direction upon thermal treatment at a temperature of 80°C for 10 seconds

and a melting point of 170°C or higher as measured by differential scanning

calorimetry.

According to an embodiment, there is provided a polyester film, which

comprises a copolymerized polyester resin comprising a diol component and a

dicarboxylic acid component, wherein the heat shrinkage rate of the film is 30% or

more in the main shrinkage direction upon thermal treatment at a temperature of 800 C

for 10 seconds, and the crystallization temperature of the film is not measured or is 700 C

to 95 0 C by differential scanning calorimetry.

According to an embodiment, the copolymerized polyester resin comprises a

diol component and a dicarboxylic acid component.

According to an embodiment, the diol component is composed of a linear or

branched C 2 to Cio diol. That is, the diol component may not comprise an alicyclic diol

or an aromatic diol.

For example, the linear or branched C 2 to C10 diol may comprise a derivative of

ethylene glycol, diethylene glycol, neopentyl glycol, 1,3-propanediol, 1,2-octanediol,

1,3-octanediol, 2,3-butanediol, 1,3-butanediol, 1,4-butanediol, 1,5-pentanediol, 2

butyl-2-ethyl-1,3-propanediol,2,2-diethyl-1,5-pentanediol,2,4-diethyl-1,5-pentanediol,

3-methyl-1,5-pentanediol, 1,1-dimethyl-1,5-pentanediol, 1,6-hexanediol, 2-ethyl-3

methyl-1,5-hexanediol, 2-ethyl-3-ethyl-1,5-hexanediol, 1,7-heptanediol, 2-ethyl-3

methyl-1,5-heptanediol, 2-ethyl-3-ethyl-1,6-heptanediol, 1,8-octanediol, 1,9

nonanediol, 1,10-decanediol, or any combination thereof. But it is not limited thereto.

According to an embodiment, the diol component may comprise at least one

selected from the group consisting of ethylene glycol, diethylene glycol, cyclohexanedimethanol (CHDM), propanediol unsubstituted or substituted with an

alkyl group, butanediol unsubstituted or substituted with an alkyl group, pentanediol

unsubstituted or substituted with an alkyl group, hexanediol unsubstituted or

substituted with an alkyl group, octanediol unsubstituted or substituted with an alkyl

group, and a combination thereof.

According to an embodiment, the diol component may comprise ethylene

glycol, diethylene glycol, 1,4-cyclohexanedimethanol, 1,3-propanediol, 1,2-octanediol,

1,3-octanediol, 2,3-butanediol, 1,3-butanediol, 1,4-butanediol, 1,5-pentanediol, neopentyl glycol, 2-butyl-2-ethyl-1,3-propanediol, 2,2-diethyl-1,5-pentanediol, 2,4

diethyl-1,5-pentanediol, 3-methyl-1,5-pentanediol, 1,1-dimethyl-1,5-pentanediol, or a

combination thereof.

According to an embodiment, the diol component may be at least one selected

from the group consisting of ethylene glycol, diethylene glycol, neopentyl glycol, and

cyclohexanedimethanol.

The dicarboxylic acid component may be selected from the group consisting

of an aromatic dicarboxylic acid such as terephthalic acid, dimethylterephthalic acid,

isophthalic acid, naphthalene dicarboxylic acid, orthophthalic acid, and the like; an

aliphatic dicarboxylic acid such as adipic acid, azelaic acid, sebacic acid, decanedicarboxylic acid, and the like; an alicyclic dicarboxylic acid; an ester thereof;

and a combination thereof. Specifically, the dicarboxylic acid component may be composed of terephthalic acid, dimethylterephthalic acid, isophthalic acid, naphthalene dicarboxylic acid, orthophthalic acid, or a combination thereof.

According to an embodiment, the dicarboxylic acid component may comprise

an aromatic dicarboxylic acid. For example, the dicarboxylic acid component may

comprise at least 80% by mole, at least 90% by mole, or at least 95% by mole of

terephthalic acid, dimethyl terephthalic acid, or isophthalic acid, based on the total

number of moles of the dicarboxylic acid component.

According to an embodiment, the copolymerized polyester resin may

comprise ethylene glycol in an amount of 55 to 94% by mole based on the total number

of moles of the diol component. For example, the copolymerized polyester resin may

comprise ethylene glycol in an amount of 60 to 90% by mole, 65 to 85% by mole, or

65 to 80% by mole, based on the total number of moles of the diol component. If the

above range is satisfied, the heat shrinkage rate of a film thus prepared can be adjusted

to a proper level, and the clumping fraction in the subsequent regeneration step can be

reduced.

According to an embodiment, the copolymerized polyester resin may

comprise diethylene glycol in an amount of 1 to 20% by mole based on the total

number of moles of the diol component. For example, the copolymerized polyester

resin may comprise diethylene glycol in an amount of 1 to 15% by mole, 1 to 13% by

mole, 1 to 10% by mole, 1.5 to 10% by mole, or 1 to 8% by mole, based on the total

number of moles of the diol component. If the above range is satisfied, the heat

shrinkage rate of a film thus prepared can be adjusted to a proper level, and the

clumping fraction in the subsequent regeneration step can be reduced.

According to an embodiment, the copolymerized polyester resin may comprise

neopentyl glycol in an amount of 5 to 35% by mole based on the total number of moles

of the diol component. For example, the copolymerized polyester resin may comprise

neopentyl glycol in an amount of 5 to 30% by mole, 7 to 35% by mole, 10 to 30% by

mole, or 15 to 30% by mole, based on the total number of moles of the diol component.

If the above range is satisfied, a polyester film having a heat shrinkage rates in a first

direction and in a direction perpendicular to the first direction that are not high even at

a high temperature can be prepared. In particular, if the content of neopentyl glycol

exceeds the above range, the film may excessively expand in the second direction as

compared with the first direction, so that wrinkles or deformation may occur when the

film is applied to a container. In addition, if the content of neopentyl glycol is less than

the above range, the amorphous region is unnecessarily large, whereby the expansion

coefficient would be increased due to the low shrinkage characteristics in the second

direction although the shrinkage characteristics in the first direction could be improved.

In this specification, the first direction is the main shrinkage direction and may

be the transverse direction or the longitudinal direction. Specifically, the first direction

may be the transverse direction, and the second direction that is perpendicular to the

first direction may be the longitudinal direction. Alternatively, the first direction may

be the longitudinal direction, and the second direction that is perpendicular to the first

direction maybe the transverse direction.

According to an embodiment, the copolymerized polyester resin may

comprise cyclohexanedimethanol in an amount of 0 to 35% by mole based on the total

number of moles of the diol component. For example, the copolymerized polyester

resin may comprise cyclohexanedimethanol in an amount of 1 to 35% by mole, 5 to 30%

by mole, 7 to 30% by mole, 10 to 30% by mole, or 15 to 30% by mole, based on the

total number of moles of the diol component. If the above range is satisfied, the heat

clumping fraction in the subsequent regeneration step can be reduced.

According to an embodiment, the copolymerized polyester resin comprises a

dicarboxylic acid component and a diol component, wherein the dicarboxylic acid

component may be composed of terephthalic acid, isophthalic acid, or dimethyl

terephthalic acid, and the diol component may be composed of (i) neopentyl glycol and

(ii) ethylene glycol, diethylene glycol, cyclohexanedimethanol, or a combination thereof. Specifically, the dicarboxylic acid component may be composed of terephthalic acid or dimethyl terephthalic acid, and the diol component may be composed of (i) neopentyl glycol and (ii) ethylene glycol. Alternatively, the dicarboxylic acid component may be composed of terephthalic acid, isophthalic acid, or dimethyl terephthalic acid, and the diol component may be composed of (i) diethylene glycol and (ii) ethylene glycol.

If the dicarboxylic acid component in the copolymerized polyester resin is

composed of a terephthalic acid, isophthalic acid, or dimethyl terephthalic acid, and if

the diol component therein is composed of (i) neopentyl glycol and (ii) ethylene glycol,

diethylene glycol, or a combination thereof, the copolymerized polyester resin may

have a reduced whitening phenomenon and a low haze of 15% or less and is excellent

in dimensional stability.

The diol component may further comprise a monohydric alcohol. For example,

it may further comprise isopropyl alcohol. Specifically, the copolymerized polyester

resin may comprise a monohydric alcohol in an amount of 15 to 30% by mole, 18 to 25%

by mole, or 20 to 25% by mole, based on the total number of moles of the diol

component. But it is not limited thereto.

The dicarboxylic acid component and the diol component as described above

are subjected to a transesterification reaction and then polymerization to thereby form a

copolymerized polyester resin. Specifically, at least one catalyst selected from

manganese acetate, calcium acetate, and zinc acetate may be used as a catalyst for the

transesterification reaction. The content of the catalyst may be 0.02 to 0.2% by weight

based on the total weight of the dicarboxylic acid compound. Upon completion of the

transesterification reaction, at least one additive selected from silica, potassium, and

magnesium; a stabilizer such as trimethyl phosphate; a polymerization catalyst selected

from antimony trioxide and tetrabutylene titanate; and the like may be selectively

added to carry out the reaction, to thereby prepare a copolymerized polyester resin

composition.

According to an embodiment, the polyester film may have a heat shrinkage

rate of 30% or more in thefirst direction upon thermal treatment at a temperature of 800 C

for 10 seconds. For example, the polyester film may have a heat shrinkage rate of 40%

or more, 45% or more, 50% or more, 30% to 85%, 40% to 80%, or 50% to 80%, in the

first direction upon thermal treatment at a temperature of 80 0C for 10 seconds. If the

above range is satisfied, it is easy to attach and label the polyester film on the surface

of a container.

According to an embodiment, the polyester film may have a heat shrinkage

rate of 50% or more in thefirst direction upon thermal treatment at a temperature of 900 C

for 10 seconds. For example, the polyester film may have a heat shrinkage rate of 55%

or more, 60% or more, 70% or more, 50% to 90%, 60% to 85%, 70% to 85%, or 70%

to 80%, in the first direction upon thermal treatment at a temperature of 900 C for 10

seconds. If the above range is satisfied, it is easy to attach and label the polyester film

on the surface of a container.

According to an embodiment, the polyester film may have a heat shrinkage

rate of 5% to 55% in thefirst direction upon thermal treatment at a temperature of 700 C

for 10 seconds. For example, the polyester film may have a heat shrinkage rate of 5%

to 50%, 10% to 50%, 20% to 45%, or 25% to 40%, in the first direction upon thermal

treatment at a temperature of 70 0C for 10 seconds. If the above range is satisfied, it is

easy to attach and label the polyester film on the surface of a container.

According to an embodiment, the polyester film may have a heat shrinkage

rate of 30% or more in the first direction upon thermal treatment at a temperature of

100 0C for 10 seconds. For example, the polyester film may have a heat shrinkage rate

of 35% or more, 40% or more, 50% or more, 30% to 90%, 30% to 80%, 40% to 80%,

45% to 80%, or 50% to 80%, in the first direction upon thermal treatment at a

temperature of 100 0C for 10 seconds. If the above range is satisfied, it is easy to attach

and label the polyester film on the surface of a container.

According to an embodiment, the rate of increase in the heat shrinkage rate in the first direction in the temperature range of 0.35 x Tm°C to 0.40 x Tm°C is 2.5%/°C to 4.0%/°C, and the rate of increase in the heat shrinkage rate in the first direction in the temperature range of 0.45 x Tm°C to 0.50 x Tm°C is 0.1%/°C to 1.0%/°C.

According to an embodiment, the polyester film has a melting point (Tm) of

170°C or higher as measured by differential scanning calorimetry. For example, the

polyester film may have a melting point of 175°C or higher, 170°C or higher,

specifically 170°C to 230°C, 170°C to 200°C, or 175°C to 200°C, as measured by

differential scanning calorimetry. If the above range is satisfied, the clumping fraction

in the subsequent regeneration step can be reduced.

According to an embodiment, the crystallization temperature of the polyester

film is not measured or is 70°C to 95°C by differential scanning calorimetry. For

example, the crystallization temperature of the polyester film may be 70°C to 93°C, 75°C

to 93°C, or 75°C to 90°C by differential scanning calorimetry. If the above range is

satisfied, the clumping fraction in the subsequent regeneration step can be reduced.

According to an embodiment, the heat of crystallization of the polyester film

may be 0.01 to 50 J/g as measured at the crystallization temperature (Tc). For example,

the heat of crystallization of the polyester film may be 0.01 to 40 J/g, 0.05 to 30 J/g, 0.1

to 20 J/g, 0.1 to 10 J/g, 0.1 to 8 J/g, or 0.1 to 5 J/g, as measured at the crystallization

temperature (Tc). If the above range is satisfied, the clumping fraction in the

subsequent regeneration step can be reduced.

According to an embodiment, the polyester film has a glass transition

temperature (Tg) of 60°C or higher as measured by differential scanning calorimetry.

For example, the polyester film may have a glass transition temperature of 65°C or

higher, 68°C or higher, 70°C or higher, 60°C to 150°C, 650 C to 1500 C, 690 C to 1500 C, 70 0C to 120 0 C, or 65 0 C to 800 C, as measured by differential scanning calorimetry. If

the above range is satisfied, the clumping fraction in the subsequent regeneration step

can be reduced.

According to an embodiment, the polyester film may have a haze of 10% or less. For example, the polyester film may have a haze of 8% or less, 7% or less, or 5% or less.

According to an embodiment, the polyester film may have a haze of 50% or

less when immersed in a 0.5% to 3% aqueous solution of NaOH for 5 minutes to 30

minutes. More specifically, the polyester film may have a haze of 10% or less, 7% or

less, 5% or less, 30% to 50%, 35% to 45%, or 40% to 45%, when immersed in a 1%

aqueous solution of NaOH for 15 minutes. For example, the polyester film may have a

haze of 9% or less, 7% or less, 5% or less, 30% to 50%, 35% to 45%, or 40% to 45%,

when immersed in a 0.5% to 2.5% or 0.5% to 2% aqueous solution of NaOH for 5

minutes to 20 minutes or 10 minutes to 15 minutes at a temperature of 70°C to 90°C,

75°C to 90°C, or 85°C. If the above range is satisfied, the clumping fraction in the

subsequent regeneration step can be reduced.

According to an embodiment, when the polyester film is immersed in a 0.5%

to 3% aqueous solution of NaOH for 5 minutes to 30 minutes, the haze difference

before and after the immersion may be 20% to 50%. For example, when the polyester

film is immersed in a 1% aqueous solution of NaOH for 15 minutes, the haze

difference before and after the immersion may be 20% to 40%, 25% to 40%, or 30% to

40%. If the above range is satisfied, the clumping fraction in the subsequent

regeneration step can be reduced.

Specifically, when the polyester film is immersed in a 1% aqueous solution of

NaOH for 15 minutes and if the haze difference before and after the immersion

satisfies 20% to 50%, the melting point may be 140°C or higher as measured by

differential scanning calorimetry. For example, when the polyester film is immersed in

a 1% aqueous solution of NaOH for 15 minutes and if the haze difference before and

after the immersion is 20% to 40%, 25% to 40%, or 30% to 40%, the melting point

may be 140°C to 230°C, 145°C to 200°C, or 150°C to 200°C, as measured by

differential scanning calorimetry.

According to an embodiment, the thickness of the polyester film may be 30 to

100 pm. For example, the thickness of the polyester film may be 30 to 95 pm or 35 to

90 pm. If the above range is satisfied, the shrinkage uniformity is excellent.

According to an embodiment, there is provided a polyester film, which

comprises a first layer comprising a copolymerized polyester resin comprising a diol

component and a dicarboxylic acid component and a second layer comprising a resin

having a glass transition temperature (Tg) of 70°C or higher.

First layer

According to an embodiment, the first layer comprises a copolymerized

polyester resin comprising a diol component and a dicarboxylic acid component.

Details on the copolymer polyester resin are as described above.

According to an embodiment, the thickness of the first layer may be 30 to 100

pm. For example, the thickness of the first layer may be 30 to 90 pm, 30 to 85 pm, 35

to 90 pm, or 40 to 80 pm.

Second layer

According to an embodiment, the second layer comprises a resin having a

glass transition temperature (Tg) of 70°C or higher. For example, the second layer may

comprise a resin having a glass transition temperature of 70°C or higher, 75°C or

higher, 80°C or higher, 70°C to 350°C, 70°C to 330°C, 70°C to 3000 C, 750 C to 2500 C, 75 0C to 200 0C, 75 0 C to 1800 C, 750 C to 1500 C, or 750 C to 1200 C.

The second layer, which contains a resin that satisfies the glass transition

temperature range, enhances the heat shrinkage rate of the polyester film and reduces

the clumping fraction in the subsequent regeneration step.

According to an embodiment, the second layer may comprise at least one resin

selected from the group consisting of polyethylene terephthalate (PET), polycyclohexylene dimethylene terephthalate (PCT), polymethylmethacrylate

(PMMA), copolymerized polyethylene terephthalate (co-PET), polyethylene

naphthalate (PEN), polyethersulfone (PES), polycarbonate (PC), polystyrene (PS),

polyamide (PA), and polyimide (PI).

According to an embodiment, the thickness of the second layer may be 1 to 100

nm. For example, the thickness of the second layer may be 1 to 80 nm, 5 to 100 nm, 10

to 100 nm, 20 to 100 nm, 20 to 50 nm, 30 to 100 nm, 20 to 50 nm, 1 to 30 nm, 5 to 10

nm, 5 to 20 nm, or 1 to 20 nm.

According to an embodiment, the polyester film may be composed of 2 to 100

layers by laminating the first layer and the second layer. For example, the polyester

film may be composed of 2 to 100 layers, 3 to 100 layers, 4 to 100 layers, 5 to 100

layers, 2 to 80 layers, 2 to 50 layers, 3 to 80 layers, 3 to 50 layers, 3 to 40 layers, or 3 to

30 layers by alternately laminating the first layer and the second layer. Specifically, at

least one of the outermost layers of the polyester film is composed of the second layer,

which is advantageous in that it is possible to reduce the clumping fraction in the

subsequent regeneration step.

According to an embodiment, the polyester film may be composed of three

layers by laminating the first layer and the second layer, wherein the second layer may

be located in the outermost layers. For example, the polyester film may be composed 3

to 80 layers, 3 to 50 layers, 3 to 40 layers, or 3 to 30 layers by alternately laminating

the first layer and the second layer, wherein at least one of the outermost layers of the

polyester film is the second layer. Specifically, the second layer, which comprises a

resin having a glass transition temperature (Tg) of 70°C or higher, is located in the

outermost layers of the polyester film, which is advantageous in that it is possible to

reduce the clumping fraction in the subsequent regeneration step.

According to an embodiment, the polyester film, which comprises the first

layer and the second layer, may have a melting point (Tm) of 150°C or higher as

measured by differential scanning calorimetry. For example, the melting point of the

polyester film may be 155°C or higher, 160°C or higher, 165°C or higher, specifically

150 0C to 230 0C, 155 0 C to 200 0 C, 160 0C to 2000 C, 165 0 C to 2000 C, or 1650 C to 1800 C,

as measured by differential scanning calorimetry. If the above range is satisfied, the

clumping fraction in the subsequent regeneration step can be reduced.

Process for preparing a polyester film (1)

A polyester film may be prepared from the copolymerized polyester resin.

Specifically, the copolymerized polyester resin may be melt-extruded at 260°C

to 300°C or 270°C to 290°C through a T-die and then cooled to obtain an unstretched

sheet. The unstretched sheet is passed through rolls while it is conveyed at a speed of

10 m/min to 110 m/min or 50 m/min to 90 m/min, preheated, and then stretched to

obtain a stretched sheet, which is heat set to prepare a polyester film.

The preheating may be carried out at 90 0 C to 120 0C for 0.01 to 1 minute. For

example, the preheating temperature (T) may be 95 0 C to 1150 C or 970 C to 1130 C, and

the preheating time may be 0.05 minute to 0.5 minute or 0.08 minute to 0.2 minute. But

they are not limited thereto.

According to an embodiment, the stretching may be carried out in a first

direction or in a second direction perpendicular to the first direction. Alternatively, the

stretching may be carried out in a first direction and then in a second direction.

Specifically, the stretching may be carried out at a temperature lower than the

preheating temperature (T) by at least 20 0C in a first direction or in a second direction

perpendicular to the first direction by 3 to 5 times. For example, the stretching may be

carried out at a stretching temperature of 600 C to 900 C, 700 C to 900 C, or 800 C to 90C,

in a first direction or in a second direction perpendicular to the first direction by 3 to

4.5 times, 3.5 to 4.5 times, or 4 to 4.5 times. But it is not limited thereto.

The heat setting may be annealing and carried out at 700 C to 950 C for 0.01

minute to 1 minute. For example, the heat setting temperature (T2) may be 750 C to

95 0C, 75 0C to 900 C, 800 C to 900 C, 850 C to 95C, or 85C to 90C, and the heat setting

time may be 0.05 minute to 0.5 minute or 0.08 minute to 0.2 minute. But they are not

limited thereto.

According to an embodiment, the preheating temperature (Ti) - the heat setting

temperature (T2) may be 10 0C to 40 0C. For example, T1 - T2 may be 130 C to 350 C, 110 C

to 34 0 C, 15 0C to 34 0C, or 20 0C to 340 C. If the above range is satisfied, the heat shrinkage rates in the first direction and in the second direction may be effectively controlled.

Process for preparing a polyester film (2)

A polyester film may be prepared from the copolymerized polyester resin and

a resin having a glass transition temperature (Tg) of 70°C or higher.

Specifically, the process may comprise (a) preparing a sheet in which a first

layer and a second layer are laminated from the copolymerized polyester resin and a

resin having a glass transition temperature (Tg) of 70°C or higher; (b) stretching the

laminated sheet in at least one of a first direction and a second direction perpendicular

to the first direction; (c) heat setting the stretched sheet; and (d) relaxing the heat-set

sheet.

Step (a)

According to an embodiment, a sheet in which a first layer and a second layer

are laminated may be prepared. Specifically, the copolymerized polyester resin and a

resin having a glass transition temperature (Tg) of 70°C or higher may be melt

extruded through an extruder, or the copolymerized polyester resin is melt-extruded

and then a resin having a glass transition temperature (Tg) of 70°C or higher is coated

thereon, which is then dried to prepare a sheet in which a first layer and a second layer

are alternately laminated. More specifically, the sheet prepared in the step (a) may be

prepared by co-extruding the copolymerized polyester resin and a resin having a glass

transition temperature (Tg) of 70°C or higher, or extruding the copolymerized polyester

resin, which is then subjected to a coating step to prepare a sheet in which a first layer

and a second layer are laminated. The co-extrusion or coating step may be carried out

by a conventional step.

According to an embodiment, the formation and lamination of the first layer

and the second layer maybe carried out simultaneously through co-extrusion.

According to an embodiment, the sheet prepared in the step (a) may be one in

which the first layer and the second layer are alternately laminated. In addition, the outermost layers of the sheet prepared in the step (a) may be the second layer.

The melt-extrusion may be carried out at a temperature of 260°C to 300°C or

270°C to 290°C. The melt-extruded copolymerized polyester resin and the resin having

a glass transition temperature (Tg) of 70°C or higher may be laminated through a

multilayer feed block to form a sheet. Alternatively, the copolymerized polyester resin

and the resin having a glass transition temperature (Tg) of 70°C or higher may be

extruded through two extruders, respectively, to a plurality of layers, which, as

laminated, is then led to a T-die to form a sheet.

Step (b)

According to an embodiment, in the step (b), a step of stretching the sheet

may be carried out in at least one of a first direction or a second direction perpendicular

to the first direction.

Specifically, the sheet may be preheated at 90°C to 140°C for 0.01 minute to 1

minute before the stretching. For example, the preheating temperature (Ti) may be 95°C

to 115°C or 97°C to 113°C, and the preheating time may be 0.05 minute to 0.5 minute

or 0.08 minute to 0.2 minute. But they are not limited thereto.

The stretching may be carried out by biaxial stretching. For example, it may

be carried out in a first direction and in a second direction through a simultaneous

biaxial stretching method or a sequential biaxial stretching method. Preferably, it may

be carried out by a sequential biaxial stretching method in which stretching is first

performed in one direction and then stretching is performed in the direction

perpendicular thereto. For example, the sheet may be stretched in a first direction and

then stretched in a second direction.

According to an embodiment, the stretching may be carried out in a first

Specifically, the stretching may be carried out at a temperature lower than the

preheating temperature (T) by at least 20°C in a first direction or in a second direction perpendicular to the first direction by 3 to 5 times. For example, the stretching may be carried out at a stretching temperature of 600 C tol200 C, 600 C to 900 C, 700 C to 900 C, or

80 0C to 90 0C, in a first direction or in a second direction perpendicular to the first

direction by 3 to 4.5 times, 3.5 to 4.5 times, or 4 to 4.5 times. But it is not limited

thereto.

Step (c)

According to an embodiment, in the step (c), the stretched sheet may be heat set.

Specifically, the heat setting may be annealing and carried out at 700 C to 950 C

for 0.01 minute to 1 minute. For example, the heat setting temperature (T2) may be 750 C

to 95 0 C or 75 0 C to 90 0 C, and the heat setting time may be 0.05 minute to 0.5 minute or

0.08 minute to 0.2 minute. But they are not limited thereto.

According to an embodiment, the preheating temperature (Ti) - the heat setting

temperature (T2) may be 10 0C to 50 0C. For example, T1 - T2 may be 130 C to 350 C, 100 C

to 34 0 C, 15 0 C to 34 0 C, 10 0C to 46 0 C, or 20 0 C to 460 C. If the above range is satisfied,

the heat shrinkage rates in the first direction and in the second direction may be

effectively controlled.

Step (d)

According to an embodiment, in the step (d), the heat-set sheet may be relaxed.

Specifically, the heat-set sheet may be relaxed in a first direction or in a second

direction perpendicular to the first direction.

The relaxation may be carried out at a relaxation rate of 0.1% to 10%, 0.5% to

8%, 1% to 5%, or 1% to 3%. In addition, the relaxation may be carried out for 1 second

to 1 minute, 2 seconds to 30 seconds, or 3 seconds to 10 seconds.

Process for Regenerating a Polyester Container

According to an embodiment, there is provided a process for regenerating a

flakes; and thermally treating the flakes to produce regenerated polyester chips, wherein when the flakes are thermally treated at a temperature of 2000 C to 2200 C for

the polyester film.

Fig. 1 schematically depicts a process for regenerating a polyester container

according to an embodiment. Specifically, Fig. 1 illustrates (1) preparing a polyester

container provided with a polyester film; (2) crushing the container provided with the

polyester film to obtain flakes; and (3) thermally treating the flakes to produce

regenerated polyester chips.

Step (1)

In the step (1), a polyester container provided with a polyester film is prepared.

Specifically, in the step (1), a waste polyester container provided with a polyester film

is prepared.

Details on the polyester film are as described above.

In the polyester container provided with a polyester film, the polyester film

may be provided on the outer surface of the polyester container. Specifically, the outer

surface of the container is covered with the polyester film, and the polyester film may

be shrunk by steam or hot air to wrap the outer surface of the container. In such event,

the polyester film may have an ink layer formed by a process such as printing before

the heat shrinkage.

According to an embodiment, the second layer of the polyester film provided

in the polyester container may be in contact with the polyester container. For example,

when the polyester film is a laminated film of the first layer and the second layer, the

second layer may be in contact with the polyester container. If the second layer of the

polyester film is in contact with the polyester container, it is possible to reduce the

clumping fraction in the subsequent regeneration step.

In general, recycled waste products are intermingled with containers, metals,

glass, and plastics. Once the waste products have been washed, polyester containers are classified. Then, the container may be subject to a process in which the film covering the container is mechanically torn or cut to be removed. Alternatively, once a container has been washed and crushed, it is then subjected to liquid specific gravity separation, dehydration, drying, and/or wind specific gravity separation, and then to such an additional step as pelletization. In such event, the quality of the regenerated polyester chips to be produced may be deteriorated due to the residual films and the ink layer formed on the residual films.

In contrast, it is possible to produce regenerated polyester chips from a

container provided with a polyester film according to the embodiment even without an

additional process of removing a film. Thus, time and cost are saved.

According to an embodiment, the polyester container may comprise at least 90%

by weight of a polyester resin based on the total weight of the polyester container.

Specifically, the polyester container may be a container that comprises polyethylene

terephthalate and may comprise polyethylene terephthalate in an amount of 90% by

weight or more, 95% by weight or more, or 99% by weight or more, based on the total

weight of the polyester container.

According to an embodiment, the process may comprise immersing the

polyester container provided with the film in a 0.5% to 3% aqueous solution of NaOH

for 5 minutes to 30 minutes. For example, the process may comprise immersing the

polyester container provided with the film in a 0.5% to 2.5% or 1% to 0.5% aqueous

solution of NaOH for 5 minutes to 25 minutes or 10 minutes to 20 minutes.

Step (2)

In the step (2), the polyester container provided with the polyester film is

crushed to obtain flakes. The polyester container prepared in the step (1) comprises the

polyester film, which may be crushed to obtain flakes. In such event, the flakes

comprise first flakes obtained by crushing the polyester container and second flakes

obtained by crushing the polyester film.

According to an embodiment, the particle size of the first flakes may be 0.1 to

20 mm, and the particle size of the second flakes may be 0.1 to 20mm. For example,

the particle size of the first flakes may be 0.5 to 15 mm, 1 to 15 mm, or 2 to 10 mm,

and the particle size of the second flakes may be 0.5 to 15 mm, 1 to 15 mm, or 2 to 10

mm.

Step (3)

In the step (3), the flakes are thermally treated to produce regenerated

polyester chips.

The thermal treatment may be carried out at 200°C to 220°C for 60 minutes to

120 minutes. For example, the thermal treatment may be carried out at 2000 C to 2150 C

or 205 0C to 220 0 C for 70 minutes to 120 minutes or 80 minutes to 120 minutes.

Regenerated polyester chips that comprise the flakes may be obtained after the

thermal treatment step. Specifically, regenerated polyester chips that comprise the first

flakes and the second flakes may be obtained. For example, the flakes may be melt

extruded and cut to obtain regenerated polyester chips.

According to an embodiment, the flakes may be washed before the thermal

treatment thereof. For example, the flakes may be washed with a 0.5% to 3% aqueous

solution of NaOH at 80C to 97C for 5 minutes to 30 minutes. A part or all of the ink

layer remaining in the flakes may be removed by carrying out the washing.

According to an embodiment, the flakes may be dried at 600 C to 1750 C for 10

minutes to 30 minutes after the washing step.

Regenerated Polyester Chips

According to an embodiment, the regenerated polyester chips may comprise

first flakes comprising polyethylene terephthalate and second flakes comprising a

copolymerized polyester resin.

According to an embodiment, the regenerated polyester chips may have an

intrinsic viscosity (IV) of 0.60 dl/g or more. For example, the regenerated polyester

chips may have an intrinsic viscosity (IV) of 0.63 dl/g or more, 0.65 dl/g or more, 0.70

dl/g or more, 0.75 dl/g or more, 0.60 to 3.00 dl/g, 0.60 to 2.0 dl/g, or 0.65 to 1.0 dl/g.

According to an embodiment, when the flakes are thermally treated at a

temperature of 200°C to 220°C for 60 minutes to 120 minutes, the clumping fraction

may be 8% or less. More specifically, when the flakes are thermally treated at a

temperature of 210°C for 90 minutes, the clumping fraction may be 8% or less, 6% or

less, 5% or less, 4% or less, 3% or less, 2% or less, 0.1% to 8%, 0.5% to 6%, or 1% to

6%. For example, when the flakes are thermally treated at a temperature of 200°C to

220°C for 60 minutes to 120 minutes, the clumping fraction may be 8% or less, 6% or

less, 5% or less, 4% or less, 3% or less, 2% or less, 0.1% to 8%, 0.5% to 6%, 1% to 6%,

or 1% to 5%.

The clumping refers to an aggregate that may be formed from the flakes. The

size of the aggregate may be, for example, at least three times the size of the flake

particle. The clumping fraction refers to the fraction of aggregates based on the total

weight of the flakes. For example, the flakes may be passed through a sieve and

thermally treated. At that time, aggregates may be formed as the flakes are clumped.

The aggregates may be passed through a sieve again to be separated. The weight of the

aggregates thus obtained isa measured to calculate the weight ratio of the aggregates

based on the total weight of the thermally treated flakes as the clumping fraction.

Thus, the higher the value of the crumbling fraction is, the more the first

flakes and the second flakes are entangled together to lower the quality of the

regenerated chips. However, the second flakes are obtained by crushing the polyester

film according to the embodiment, thereby effectively reducing or preventing the

clumping phenomenon and enhancing the quality of the regenerated polyester chips.

According to an embodiment, the regenerated polyester chips may comprise

70 to 99% by weight of polyethylene terephthalate and 1 to 30% by weight of a

copolymerized polyester resin based on the total weight of regenerated polyester chips.

For example, the regenerated polyester chips may comprise 80 to 99% by weight, 90 to

99% by weight, or 95 to 99% by weight of polyethylene terephthalate and 1 to 28% by

weight or 3 to 25% by weight of a copolymerized polyester resin based on the total weight of the regenerated polyester chips.

Details on the copolymer polyester resin are as described above.

Mode for the Invention

Hereinafter, the present invention will be described in more detail with

reference to the following examples. However, these examples are set forth to illustrate

the present invention, and the scope of the present invention is not limited thereto.

[Example 1-1]

A stainless steel autoclave equipped with a stirrer, a thermometer, and a

partial reflux condenser was charged with 100% by mole of dimethylterephthalate

(DMT), 80% by mole of ethylene glycol (EG), 15% by mole of neopentyl glycol

(NPG), and 5% by mole of diethylene glycol (DEG). Then, 0.05% by mole (based on

the acid component) of zinc acetate as a transesterification catalyst was added thereto.

The transesterification reaction was carried out while methanol was being distilled off.

Thereafter, 0.025% by mole (based on the acid component) of antimony trioxide as a

polycondensation catalyst was added, and the polycondensation reaction was carried

out under a reduced pressure of 26.6 Pa (0.2 Torr) at 280°C to obtain a copolymerized

polyester resin.

The copolymerized polyester resin was fed to an extruder and then melt

extruded at 280°C through a T-die. Thereafter, it was wound around a rotating metal

roll whose surface temperature was cooled to 30°C to obtain an unstretched film

having a thickness of 204 pm. Here, the take-up speed (rotation speed of the metal roll)

of the unstretched film was 54 m/min.

The unstretched film was continuously wound around a plurality of rotating

rolls to be preheated. The longitudinally stretched film was stretched 5 times in the

transverse direction at 96°C. Thereafter, the film was heat set in the transverse direction while it was heated to 81°C using an infrared heater to obtain a polyester film having a thickness of 41 pm.

The outer surface of a polyethylene terephthalate container (PET container, 30

g) was wrapped with the polyester film (1 g) prepared above. The polyester film was

shrunk in hot air at a temperature of 90°C to obtain a polyester container provided with

a polyester film.

The container provided with the polyester film was crushed with a crusher to

obtain flakes. The flakes were washed with water and then washed for 15 minutes with

a corrosion washing solution (a mixture of a solution of 0.3% by weight of Triton X

100 and a solution of 1.0% by weight of NaOH) stirred in a bath at 850 C to 900 C at 880

rpm.

Thereafter, the flakes were washed with water at room temperature to remove

the residual corrosion washing solution, dried at 160 0C for 20 minutes, and then

thermally treated at 2100 C to produce regenerated polyester chips.

[Examples 1-2 to 1-4 and Comparative Example 1-1]

Regenerated polyester chips were prepared in the same manner as in Example

1-1, except that the components, contents, and heat-setting temperature were changed

as shown in Table 1 below.

[Table 1] Stretching DMT EG NPG DEG CHDM Heat-setting temperature in the Ha-etn (% by (% by (% by (% by (% by temperature transverse direction mole) mole) mole) mole) mole) (0C) (0C) Ex. 1-1 100 80 15 5 - 96 81 Ex. 1-2 100 70 25 5 - 96 81 Ex. 1-3 100 70 25 5 - 96 78 Ex. 1-4 100 70 25 5 - 96 75 C.Ex. 100 70 - 5 25 96 81

1-1

*CHDM: cyclohexanedimethanol

[Examples 2-1 to 2-4 and Comparative Examples 2-1]

Regenerated polyester chips were prepared in the same manner as in Example

as shown in Table 2 below.

[Table 2]

DMT EG NPG DEG CHDM Stretching Heat-setting temperature in the (% by (% by (% by (% by (% by temperature transverse direction mole) mole) mole) mole) mole) (0 C) (0 C) Ex.2-1 100 80 15 5 - 96 81 Ex.2-2 100 75 20 5 - 96 81 Ex.2-3 100 70 25 5 - 96 81 Ex.2-4 100 70 30 5 - 96 81 C. Ex. 100 70 - 5 25 96 81 2-1

[Example 3-1]

A stainless steel autoclave equipped with a stirrer, a thermometer, and a

partial reflux condenser was charged with 100% by mole of terephthalic acid (TA) as a

dicarboxylic acid component and 80% by mole of ethylene glycol (EG), 17% by mole

of neopentyl glycol (NPG), and 5% by mole of diethylene glycol (DEG) as a diol

component. Then, 0.05% by mole (based on the acid component) of zinc acetate as a

transesterification catalyst was added thereto. The transesterification reaction was

carried out while methanol was being distilled off. Thereafter, 0.025% by mole (based

on the acid component) of antimony trioxide as a polycondensation catalyst was added,

and the polycondensation reaction was carried out under a reduced pressure of 26.6 Pa

(0.2 Torr) at 280°C to obtain a copolymerized polyester resin.

The copolymerized polyester resin was fed to an extruder and then melt

of the unstretched film was 54 m/min.

The unstretched film was continuously wound around a plurality of rotating

rolls to be preheated at 1000 C to 1100 C for 0.1 minute. The longitudinally stretched

film was stretched 5 times in the transverse direction at 750 C. Thereafter, the film was

annealed in the second direction while it was heated to 850 C using an infrared heater to

obtain a polyester film having a thickness of 40 pm.

The outer surface of a polyethylene terephthalate container (PET container, 30

shrunk in hot air at a temperature of 900 C to obtain a polyester container provided with

a polyester film.

The container provided with the polyester film was crushed with a crusher to

rpm.

Thereafter, the flakes were washed with water at room temperature to remove

thermally treated at 2100 C to produce regenerated polyester chips.

[Examples 3-2 to 3-5 and Comparative Example 3-1]

Regenerated polyester chips were prepared in the same manner as in Example

3-1, except that the components, contents, and heat-setting temperature were changed

as shown in Table 3 below.

[Table 3] Stretching TA EG NPG DEG CHDM Heat-setting temperature in the (% by (% by (% by (% by (% by temperature transverse direction mole) mole) mole) mole) mole) (0C) (°C) Ex.3-1 100 80 17 5 - 75 85 Ex. 3-2 100 75 20 5 - 76 85 Ex. 3-3 100 70 25 5 - 76 83 Ex. 3-4 100 68.5 30 1.5 - 77 85 Ex. 3-5 100 73 - 10 17 75 86 C. Ex. 100 68.5 - 1.5 30 76 84 3-1

[Example 4-1]

A stainless steel autoclave equipped with a stirrer, a thermometer, and a

dicarboxylic acid component and 68.5% by mole of ethylene glycol (EG), 30% by

mole of cyclohexanedimethanol (CHDM), and 1.5% by mole of diethylene glycol

(DEG) as a diol component. Then, 0.05% by mole (based on the acid component) of

zinc acetate as a transesterification catalyst was added thereto. The transesterification

reaction was carried out while methanol was being distilled off. Thereafter, 0.025% by

mole (based on the acid component) of antimony trioxide as a polycondensation

catalyst was added, and the polycondensation reaction was carried out under a reduced

pressure of 26.6 Pa (0.2 Torr) at 280°C to obtain a copolymerized polyester resin.

The copolymerized polyester resin was fed to an extruder, melt-extruded at

280°C through a T-die, and then cooled. Polyethylene terephthalate (PET 1) having a

glass transition temperature of 70°C or higher was coated thereon to obtain an unstretched sheet. The unstretched sheet was preheated at 100°C to 110°C for 0.1 minute while it was conveyed at a speed of 55 m/min, stretched 3.0 times in the transverse direction at 75°C, and then heat set at 75°C for 0.1 minute to obtain a polyester film having a thickness of 40 pm.

The outer surface of a polyethylene terephthalate container (PET container, 30

a polyester film. At that time, the second layer of the polyester film was brought into

contact with the polyethylene terephthalate container.

The container provided with the polyester film was crushed with a crusher to

100 and a solution of 1.0% by weight of NaOH) stirred in a bath at 85°C to 90°C at 880

rpm.

Thereafter, the flakes were washed with water at room temperature to remove

the residual corrosion washing solution, dried at 160°C for 20 minutes, and then

thermally treated at 210°C to produce regenerated polyester chips.

[Examples 4-2 to 4-8 and Comparative Examples 4-1 to 4-2]

Regenerated polyester chips were prepared in the same manner as in Example

4-1, except that the components, contents, and heat-setting temperature were changed

as shown in Table 4 below and that a copolymerized polyester resin and a resin having

a glass transition temperature (Tg) of 70°C or higher were co-extruded through two

extruders and laminated in Examples 4-3, 4-4, 4-7, and 4-8.

[Table 4] 1st layer Stretching Heat No. of temperature setting .aia TA EG NPG DEG CHDM 2nd inh tep ains (% by (% by (% by (% by (% by layer t e te tions transverse rature mole) mole) mole) mole) mole) direction (C) (°C) Ex. 4-1 100 68.5 - 1.5 30 PET 1 85 75 Ex.4-2 100 65 30 5 - PET2 84 74 2 layers Ex. 4-3 100 68.5 - 1.5 30 PCT 85 75 Ex. 4-4 100 65 30 5 - PEN 84 74 Ex. 4-5 100 68.5 - 1.5 30 PET 1 85 75 Ex.4-6 100 65 30 5 - PET2 84 74 3 layers Ex. 4-7 100 68.5 - 1.5 30 PCT 96 75 Ex. 4-8 100 65 30 5 - PEN 120 74

C. Ex. Single 100 68.5 - 1.5 30 - 85 75 4-1 layer

C. Ex. Single 100 65 30 5 - - 84 74 4-2 layer

*NPG: neopentyl glycol

*PET 1: polyethylene terephthalate (Goo Chemical, Z687) (glass transition

temperature (Tg): 100°C)

*PET 2: polyethylene terephthalate (Goo Chemical, Z690) (glass transition

temperature (Tg): 110°C)

*PCT: polycyclohexylenedimethylene terephthalate (glass transition

temperature (Tg): 96°C)

*PEN: polyethylene naphthalate (glass transition temperature (Tg): 120°C)

* Lamination structure of two layers: second layer / first layer

* Lamination structure of three layers: second layer / first layer / second layer

[Evaluation Example 1: Evaluation of heat shrinkage rates]

The polyester films prepared above (300 mm x 15mm) were immersed in a water bath preheated to 80°C, 90°C, or 100°C for 10 seconds, respectively. After water was removed at room temperature, the heat shrinkage rate was calculated by the following equation.

Heat shrinkage rate (%)= (length of film sample before thermal treatment

(mm) - length of film sample upon thermal treatment (mm) / length of film sample

before thermal treatment (mm)] x 100

[Evaluation Example 2: Evaluation of Tg, Tc, Tm, and heat of

crystallization]

The endotherm and exotherm of the polyester films (10 mg) prepared above

were each measured with Differential Scanning Calorimetry-Mettler Toledo DSC 1

while the temperature was raised at a rate of 10°C/min from 30°C to 250°C. The first

endothermic temperature was a glass transition temperature (Tg), the exothermic

temperature measured after the Tg was a crystallization temperature (Tc), and the

endothermic temperature measured after the Tc was a melting point (Tm) in the

measurement result. The integral at Tc was calculated as the heat of crystallization. The

larger the value of the heat of crystallization, the faster the crystallization rate and the

higher the transfer rate to a crystalline phase.

[Evaluation Example 3: Evaluation of clumping]

The flakes prepared above were passed through a 0.625"-sieve. 1 kg of the

flakes thus sieved was exposed in an oven at 210°C for 90 minutes. They were cooled

to room temperature and passed through a 625"-sieve. The weight of the aggregates

thus filtered was measured and calculated as a percentage of the total weight of the

flakes.

[Evaluation Example 4: Evaluation of intrinsic viscosity]

The regenerated polyester chips prepared above were dissolved in ortho

chlorophenol at 100°C, and the intrinsic viscosity (IV) was measured with an Ostwald

viscometer at 35°C in a thermostatic bath by measuring the time for the sample to drop.

[Evaluation Example 5: Evaluation of haze]

The films prepared above were each immersed in a 1% aqueous solution of

NaOH at 85°C for 15 minutes. The hazes before and after the immersion were

measured with a haze meter (model name: SEP-H) from Nihon Semitsu Kogaku (Japan)

using a C-light source.

[Table 5] Heat shrinkage Heat shrinkage Heat of rate in rate TiClump- Intrinsic Tc Tm crystalli transverse transverse ing viscosity (°C) (°C) zation direction direction (%) (dl/g)

(800 C) (900 C)

Ex. 1-1 58% 70% - 199 - 0.02 0.76

Ex. 1-2 65% 78% - 171 - 1.3 0.78

Ex. 1-3 62% 79% 90 171 0.3 0.5 0.79 Ex. 1-4 67% 79% 78 - 1.2 0 0.76 C. Ex. 1-1 68% 78% 82 166 0.1 9.7 0.76

[Table 6] Heat shrinkage Heat shrinkage Heat of rate in rate TiClump- Intrinsic Tc Tm crystalli transverse transverse ing viscosity (°C) (°C) zation in vscit direction direction (%) (dl/g) (J/g) (800 C) (900 C)

Ex. 2-1 58% 70% - 199 - 0.02 0.76

Ex. 2-2 63% 72% - 178 - 0.15 0.80 Ex. 2-3 65% 78% - 171 0.3 1.3 0.78 Ex. 2-4 66% 79% - 172 1.2 4.0 0.79 C. Ex. 2-1 68% 78% 82 166 0.1 9.7 0.76

[Table 7] Heat Heat Haze shrinkage shrinkage (%) Clump- Intrinsic rate in rate in Tc Tm Before After ing viscosity transverse transverse (0 C) (0 C) ( (dl/g) direction direction

(800 C) (900 C)

Ex. 3-1 40% 60% 5 5 - 200 0.2 0.61

Ex. 3-2 45% 66% 5 5 - 180 0.5 0.62 Ex. 3-3 43% 63% 5 41 80 150 0.8 0.59 Ex. 3-4 49% 69% 6 40 79 150 1 0.57 Ex. 3-5 44% 65% 4 4 - 176 2 0.69 C. Ex. 3-1 50% 70% 3 3 - 165 10 0.71

As shown in Tables 5 to 7, the polyester films prepared in the Examples and

the regenerated polyester chips prepared by the process for regenerating a polyester

container using the same each had a low clumping fraction and were excellent in all of

the heat of crystallization and intrinsic viscosity characteristics.

[Table 8]

Heat shrinkage rate in Heat of Intrinsic Tc Tm Clumping transversedirection Crystallization viscosity (°C) (°C) (%) (100 0C) (J/g) (dl/g)

Ex. 4-1 78% - 165 - 8 0.68 Ex. 4-2 78% - 170 - 6 0.80 Ex. 4-3 60% - 165 - 5 0.68 Ex. 4-4 50% - 170 - 3 0.80 Ex. 4-5 75% - 165 - 4 0.69 Ex. 4-6 76% - 170 - 4 0.79 Ex. 4-7 55% - 165 - 2 0.75 Ex. 4-8 45% - 170 - 1 0.86

C. Ex. 4-1 78% - 165 - 10 0.68

C. Ex. 4-2 79% - 170 - 8 0.68

As shown in Table 8, the polyester films prepared in the Examples and the

regenerated polyester chips prepared by the process for regenerating a polyester

container using the same each had a low clumping fraction.

Claims

1. A polyester film, which comprises a copolymerized polyester resin comprising a diol component and a dicarboxylic acid component and has a heat shrinkage rate of 30% or more in the main shrinkage direction upon thermal treatment at a temperature of 80°C for 10 seconds and a melting point of 170°C or higher as measured by differential scanning calorimetry, wherein the crystallization temperature of the polyester film is not measured or is 70°C to 95°C by differential scanning calorimetry, wherein the heat of crystallization of the polyester film at the crystallization temperature is not measured or is 0.01 to 50 J/g, and wherein the copolymerized polyester resin comprises ethylene glycol in an amount of 55 to 94% by mole based on the total number of moles of the diol component.

2. The polyester film of claim 1, wherein the diol component is at least one selected from the group consisting of ethylene glycol, diethylene glycol, neopentyl glycol, and cyclohexanedimethanol.

3. The polyester film of claim 1 or claim 2, wherein the copolymerized polyester resin comprises ethylene glycol in an amount of 55 to 94% by mole and diethylene glycol in an amount of 1 to 20% by mole based on the total number of moles of the diol component.

4. The polyester film of any one of claims 1 to 3, wherein the copolymerized polyester resin comprises neopentyl glycol in an amount of 5 to 35% by mole based on the total number of moles of the diol component.

5. The polyester film of any one of claims 1 to 4, which has a heat shrinkage rate of 30% or more in a first direction upon thermal treatment at a temperature of 100 0C for 10 seconds, a heat shrinkage rate of 50% or more in the first direction upon thermal treatment at a temperature of 900 C for 10 seconds, and a heat shrinkage rate of 5% to 55% in the first direction upon thermal treatment at a temperature of 700 C for 10 seconds.

6. The polyester film of any one of claims 1 to 5, wherein the rate of increase in the heat shrinkage rate in a first direction in the temperature range of 0.35 x Tm°C to 0.40 x Tm°C is 2.5%/°C to 4.0%/°C, and the rate of increase in the heat shrinkage rate in the first direction in the temperature range of 0.45 x Tm°C to 0.50 x Tm°C is 0.1%/°C to 1.0%/°C.

7. A process for regenerating a polyester container, which comprises preparing the polyester container provided with the polyester film according to any one of claims 1 to 6; crushing the container provided with the polyester film to obtain flakes; and thermally treating the flakes to produce regenerated polyester chips, wherein when the flakes are thermally treated at a temperature of 2000 C to 2200 C for 60 minutes to 120 minutes, the clumping fraction is 8% or less, and the flakes comprise first flakes obtained by crushing the container and second flakes obtained by crushing the polyester film.

8. The process for regenerating a polyester container of claim 7, wherein the particle size of the first flakes is 0.1 to 20 mm, and the particle size of the second flakes is 0.1 to 20 mm.

9. The process for regenerating a polyester container of claim 7 or claim 8, wherein the container comprises polyethylene terephthalate in an amount of 90% by weight or more.

10. Regenerated polyester chips prepared according to the regeneration process of any one of claims 7 to 9.

11. The regenerated polyester chips of claim 10, which comprise first flakes that comprise polyethylene terephthalate and second flakes that comprise a copolymerized polyester resin.

12. The regenerated polyester chips of claim 10 or claim 11, which have an intrinsic viscosity (IV) of 0.60 dl/g or more.