KR100558841B1 - Polyester films for diffusing light and manufacturing method of the same - Google Patents
Polyester films for diffusing light and manufacturing method of the same Download PDFInfo
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- KR100558841B1 KR100558841B1 KR1020000077406A KR20000077406A KR100558841B1 KR 100558841 B1 KR100558841 B1 KR 100558841B1 KR 1020000077406 A KR1020000077406 A KR 1020000077406A KR 20000077406 A KR20000077406 A KR 20000077406A KR 100558841 B1 KR100558841 B1 KR 100558841B1
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/06—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material
- B32B27/08—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material of synthetic resin
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/18—Layered products comprising a layer of synthetic resin characterised by the use of special additives
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/36—Layered products comprising a layer of synthetic resin comprising polyesters
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B37/00—Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding
- B32B37/14—Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding characterised by the properties of the layers
- B32B37/15—Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding characterised by the properties of the layers with at least one layer being manufactured and immediately laminated before reaching its stable state, e.g. in which a layer is extruded and laminated while in semi-molten state
- B32B37/153—Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding characterised by the properties of the layers with at least one layer being manufactured and immediately laminated before reaching its stable state, e.g. in which a layer is extruded and laminated while in semi-molten state at least one layer is extruded and immediately laminated while in semi-molten state
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2264/00—Composition or properties of particles which form a particulate layer or are present as additives
- B32B2264/02—Synthetic macromolecular particles
- B32B2264/0214—Particles made of materials belonging to B32B27/00
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2307/00—Properties of the layers or laminate
- B32B2307/40—Properties of the layers or laminate having particular optical properties
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2307/00—Properties of the layers or laminate
- B32B2307/50—Properties of the layers or laminate having particular mechanical properties
- B32B2307/514—Oriented
- B32B2307/518—Oriented bi-axially
Abstract
본 발명은 평활성, 내구성, 가공성 등이 우수하며, 또한 제조 비용이 적게드는 광확산용 폴리에스테르 필름을 개시한다. 본 발명에 따른 폴리에스테르 필름은 반복 단위의 60중량% 이상이 에틸렌테레프탈레이트로 이루어져 있으며 극한점도가 0.4~0.9dl/g인 제1 폴리에스테르 수지로 이루어진 제1 필름층과 평균입경이 0.3∼8㎛인 유기입자가 포함되어 있고 반복 단위의 60중량% 이상이 에틸렌테레프탈레이트로 이루어져 있으며 극한점도가 0.4 ~0.9dl/g인 제1 폴리에스테르 수지로 이루어진 제2 필름층이 공압출에 의해 적층되어 있으며, 총 연신비가 9배 이상인 것을 특징으로 한다.The present invention discloses a polyester film for light diffusion that is excellent in smoothness, durability, processability, and the like, and which is low in manufacturing cost. In the polyester film according to the present invention, at least 60% by weight of the repeating unit is made of ethylene terephthalate and has a first film layer made of a first polyester resin having an intrinsic viscosity of 0.4 to 0.9 dl / g, and an average particle diameter of 0.3 to 8. A second film layer made of a first polyester resin containing an organic particle having a diameter of 60 μm and at least 60 wt% of the repeating unit is made of ethylene terephthalate and has an intrinsic viscosity of 0.4 to 0.9 dl / g is laminated by co-extrusion. And, the total draw ratio is characterized in that more than nine times.
Description
본 발명은 각종 디스플레이용으로 사용되는 광확산 필름에 관한 것으로서, 보다 상세하게는 평활도, 및 내구성이 우수할 뿐만 아니라, 공업적으로 적은 제조 비용으로 생산이 가능하여 광고 등 각종 디스플레이용으로 사용 가능한 폴리에스테르 필름 및 그의 제조방법에 관한 것이다. The present invention relates to a light-diffusion film used for various displays, and more particularly, it is not only excellent in smoothness and durability, but also can be produced with industrially low manufacturing cost and can be used for various displays such as advertisement. An ester film and its manufacturing method are related.
일반적으로 광확산 필름은 투명한 필름에 광확산 층을 코팅하여 사용하는데, 이 경우 별도의 코팅 공정을 거쳐야 할 뿐만 아니라, 소정의 광확 특성을 유지하기 위하여 고가의 유기입자를 다량 사용해야 하기 때문에 제조 비용이 매우 높다. Generally, a light diffusion film is used by coating a light diffusion layer on a transparent film. In this case, not only a separate coating process is required but also a large amount of expensive organic particles are used to maintain a predetermined light diffusion property. Very high.
또한, 코팅 시 건조 공정에 있어서, 변형이 발생하기 쉽고, 코팅 층에 의해 컬이 발생하기 쉬워 필름의 평활도가 불량해지는 문제를 않고 있으며, 제품 용도상 코팅, 인쇄, 쉬트 성형 등 일련의 후가공 공정을 거치는데, 이 경우 코팅 층이 약하여 손상이 되기 쉽다. In addition, in the drying process during coating, deformation is easy to occur, and curling occurs due to the coating layer, so that the smoothness of the film is not deteriorated, and a series of post-processing processes such as coating, printing, sheet forming, etc. In this case, the coating layer is weak and easily damaged.
따라서 평활성, 내구성, 가공성 등의 품질이 우수할 뿐만 아니라 공업적으로 제조 비용이 매우 적게 소요되는 광확산용 폴리에스테르 필름이 요구되고 있다. Therefore, there is a demand for a light diffusion polyester film that is excellent in quality such as smoothness, durability, workability, and the like, and requires very low manufacturing cost.
따라서, 본 발명이 이루고자 하는 기술적 과제는 상기의 문제점을 해결하기 위하여 내구성, 평활성, 가공성이 우수하고 제조비용이 적게 드는 광확산용 폴리에스테르 필름을 제공하는데 있다.Therefore, the technical problem to be achieved by the present invention is to provide a light diffusion polyester film excellent in durability, smoothness, processability and low manufacturing cost in order to solve the above problems.
또한, 본 발명이 이루고자 하는 다른 기술적 과제는 상기 폴리에스테르 필름의 제조방법을 제공하는데 있다.In addition, another technical problem to be achieved by the present invention is to provide a method for producing the polyester film.
상기 기술적 과제를 달성하기 위하여, 본 발명은 반복 단위의 60중량% 이상이 에틸렌테레프탈레이트로 이루어져 있으며 극한점도가 0.4~0.9dl/g인 제1 폴리에스테르 수지로 이루어진 제1 필름층과 평균입경이 0.3∼8㎛인 유기입자가 포함되어 있고 반복 단위의 60중량% 이상이 에틸렌테레프탈레이트로 이루어져 있으며 극한점도가 0.4 ~0.9dl/g인 제1 폴리에스테르 수지로 이루어진 제2 필름층이 공압출에 의해 적층되어 있으며 총 연신비가 9배 이상인 것을 특징으로 하는 이축 배향 폴리에스테르 필름을 제공한다.In order to achieve the above technical problem, the present invention is 60% by weight or more of the repeating unit is made of ethylene terephthalate and the first film layer and the average particle diameter of the first polyester resin having an ultimate viscosity of 0.4 ~ 0.9dl / g A second film layer made of a first polyester resin containing 0.3 to 8 μm of organic particles and at least 60% by weight of the repeating unit is made of ethylene terephthalate and has an intrinsic viscosity of 0.4 to 0.9 dl / g. It is laminated | stacked and provides the biaxially-oriented polyester film characterized by the total draw ratio being 9 times or more.
상기 다른 기술적 과제를 달성하기 위하여, 본 발명은 In order to achieve the above another technical problem, the present invention
(a) 반복 단위의 60중량% 이상이 에틸렌테레프탈레이트로 이루어져 있으며 극한점도가 0.4~0.9dl/g인 제1 폴리에스테르 수지의 용융물을 압출하여 제1 필름층으로 하고, 이와 동시에 평균입경이 0.3∼8㎛인 유기입자가 포함되어 있고 반복 단위의 60중량% 이상이 에틸렌테레프탈레이트로 이루어져 있으며 극한점도가 0.4 ~0.9dl/g인 제2 폴리에스테르 수지의 용용물을 상기 제1 필름층의 어느 하나의 면 에 형성하여 제2 필름층이 되도록 공압출하여 2층으로 이루어진 미연신 필름을 제조하는 단계; 및(a) 60% by weight or more of the repeating unit is composed of ethylene terephthalate and extrudates a melt of the first polyester resin having an intrinsic viscosity of 0.4 to 0.9 dl / g to form a first film layer, and at the same time an average particle diameter of 0.3 An organic particle of ˜8 μm is contained, and 60 wt% or more of the repeating unit is made of ethylene terephthalate, and the melt of the second polyester resin having an intrinsic viscosity of 0.4 to 0.9 dl / g is obtained from any one of the first film layers. Forming an unstretched film having two layers by coextrusion to one side to form a second film layer; And
(b) 상기 미연신 필름을 총 연신비가 9배 이상이 되도록 종방향과 횡방향으로 연신하는 단계를 포함하는 것을 특징으로 하는 폴리에스테르 필름의 제조방법을 제공한다.(b) providing a method for producing a polyester film, comprising stretching the unstretched film in a longitudinal direction and a transverse direction such that a total draw ratio is 9 times or more.
본 발명은 따른 폴리에스테르 필름 및 그 제조방법에 있어서, 상기 유기입자의 함량은 전체 필름에 대하여 2 내지 15중량%인 것이 바람직하며, 이 경우의 폴리에스테르 필름은 빛투과율이 90% 이상이고, 헤이즈가 65-85%일 수 있다.In the polyester film according to the present invention and a method for producing the same, the content of the organic particles is preferably 2 to 15% by weight based on the total film, the polyester film in this case has a light transmittance of 90% or more, haze May be 65-85%.
본 발명에 따른 폴리에스테르 필름 및 그 제조방법에 있어서, 상기 유기입자의 열분해 개시온도는 270℃ 이상인 것이 바람직하며, 또한 상기 유기입자는 가교 폴리메틸메타크릴레이트, 가교 폴리스티렌 및 가교 폴리메틸메타크릴레이트와 폴리스티렌의 공중합체로 이루어진 군에서 선택되는 어느 하나 이상인 것이 바람직하다. In the polyester film and the method for producing the same according to the present invention, the thermal decomposition initiation temperature of the organic particles is preferably 270 ° C. or more, and the organic particles are crosslinked polymethylmethacrylate, crosslinked polystyrene and crosslinked polymethylmethacrylate. It is preferably at least one selected from the group consisting of copolymers of polystyrene and polystyrene.
본 발명에 따른 폴리에스테르 필름은 제조 시에 공압출에 의하여 제1 필름층의 어느 한 면에 광확산층인 제2 필름층을 적층하고 이축 연신 및 열고정하므로서 평활성, 내구성, 가공성 등이 우수하고 제조비용이 적게드는 장점을 가지고 있다.The polyester film according to the present invention has excellent smoothness, durability, workability, etc. by laminating, biaxially stretching and heat setting a second film layer, which is a light diffusion layer, on either side of the first film layer by co-extrusion during manufacture. It has the advantage of low cost.
이하, 본 발명에 따른 폴리에스테르 필름 및 그 제조방법을 상세히 설명하기고 한다.Hereinafter, the polyester film according to the present invention and its manufacturing method will be described in detail.
본 발명에 따른 상기 폴리에스테르 필름의 제1 필름층과 제2 필름층을 이루어는 폴리에스테르 수지는 반복단위의 60중량% 이상이 에틸렌테레프탈레이트로 이 루어져 있다. In the polyester resin constituting the first film layer and the second film layer of the polyester film according to the present invention, at least 60% by weight of the repeating unit is made of ethylene terephthalate.
이러한 에틸렌테레프탈레이트 단위는 테레프탈산과 에틸렌글리콜의 직접에스테르화반응 또는 디메틸테레프탈레이트와 에틸렌그리콜의 에스테르교환반응에 의하여 형성될 수 있다. Such ethylene terephthalate units may be formed by direct esterification of terephthalic acid with ethylene glycol or transesterification of dimethyl terephthalate with ethylene glycol.
나머지 40중량% 이내는 공중합하여도 무방하며, 공중합성분으로는 산성분 또는 알콜 성분 모두 사용가능하다. 산성분으로서는 디메틸테레프탈산, 테레프탈산, 이소프탈산, 나프탈렌 디카르복실산, 사이클로헥산, 디카르복실산, 디페녹시에탄 디카르복실산, 안트라센 디카르복실산, αβ-비스(2-클로로페녹시)에탄-4,4-디카르복실산 등을 들 수 있으며, 알콜 성분으로는 에틸렌글리콜, 트리메틸렌글리콜 테트라메틸렌글리콜, 펜타메틸렌글리콜, 헥사메틸렌글리콜, 헥실렌글리콜 등을 들 수 있다. The remaining 40% by weight may be copolymerized, and both acid and alcohol components may be used as the copolymerization component. As the acid component, dimethyl terephthalic acid, terephthalic acid, isophthalic acid, naphthalene dicarboxylic acid, cyclohexane, dicarboxylic acid, diphenoxyethane dicarboxylic acid, anthracene dicarboxylic acid, αβ-bis (2-chlorophenoxy) And ethane-4,4-dicarboxylic acid. Examples of the alcohol component include ethylene glycol, trimethylene glycol tetramethylene glycol, pentamethylene glycol, hexamethylene glycol, and hexylene glycol.
또한, 본 발명에서 사용되는 폴리에스테르 수지는 35℃에서 오르토클로로페놀 25㎖당 0.3g의 농도로 측정한 극한점도가 0.4내지 0.9dl/g 범위에 있는 것이 바람직하고, 0.5내지 0.8dl/g의 범위가 특히 바람직하다. 만일 극한점도가 0.4dl/g 미만인 폴리에스테르로 필름을 제작하면 연신 중 파단이 빈번히 발생하여 생산성이 크게 저하될 뿐 아니라 최종 필름에서 기계적 강도 등 물성의 저하가 일어나 바람직하지 않다. 또한 극한점도가 0.9dl/g을 초과할 경우에는 용융점도가 매우 상승하고, 이에 따른 전단 응력의 증가로 압출 불안정 등 제조 공정 상 어려움이 발생하여 후 공정에서의 생산성이 크게 저하되므로 역시 바람직하지 않다. In addition, the polyester resin used in the present invention preferably has an intrinsic viscosity measured at a concentration of 0.3 g per 25 ml of orthochlorophenol at 35 ° C. in the range of 0.4 to 0.9 dl / g, and preferably 0.5 to 0.8 dl / g. Range is particularly preferred. If the film is made of polyester having an intrinsic viscosity of less than 0.4 dl / g, breakage occurs frequently during stretching, which greatly lowers the productivity, and lowers physical properties such as mechanical strength in the final film. In addition, when the intrinsic viscosity exceeds 0.9 dl / g, the melt viscosity is very high, it is not preferable because the increase in shear stress caused difficulties in the manufacturing process, such as extrusion instability, which greatly reduces the productivity in the post-process .
또한, 광확산층이 되는 제2 필름층의 제조에 사용되는 제2 폴리에스테르 수 지에는 0.3 내지 8㎛의 평균입경을 가진 유기입자가 포함된다. 상기 유기입자의 더욱 바람직한 평균입경은 0.5 내지 3㎛이다. 이는 유기입자의 평균 크기에 따른 산란 효과의 차이에 의해 광확산 효과가 달라지기 때문이다. In addition, the second polyester resin used in the production of the second film layer to be the light diffusion layer includes organic particles having an average particle diameter of 0.3 to 8㎛. More preferable average particle diameter of the said organic particle | grain is 0.5-3 micrometers. This is because the light diffusion effect is changed by the difference in the scattering effect according to the average size of the organic particles.
입자가 너무 크거나 간격이 너무 좁으면 회절이 거의 일어나지 않을 뿐만 아니라, 과도한 보이드의 형성으로 공정성 및 필름 물성의 저하를 초래하는 문제점과 반대로 입자가 너무 작으면 빛이 무기물 입자를 인식하지 못하고 그냥 통과하여 버리며, 보이드의 형성도 적어 소정의 휘도와 은폐력을 유지하기 위해서는 고가인 유기 첨가제의 함량을 높여야 하는 문제점이 발생한다. 본 발명에서는 이를 고려하여 상술한 바와 같은 평균 입경을 가진 유기입자를 사용하게 된 것이다.If the particles are too large or the spacing is too small, the diffraction hardly occurs, and if the particles are too small, the light will not recognize the inorganic particles and will just pass, as opposed to the problem of excessive void formation resulting in deterioration of fairness and film properties. In addition, the voids are also less formed, so in order to maintain a predetermined brightness and hiding power, a problem arises in that the content of expensive organic additives must be increased. In the present invention, it is to use the organic particles having an average particle diameter as described above in consideration of this.
또한, 필름 제조시 용융압출 공정의 온도가 260℃ 이상이기 때문에 유기 첨가제의 내열성은 그 이상의 것을 유지해야 하는데, 이러한 온도 조건 범위에서 내열성을 갖기 위해서는 가교된 유기 첨가제를 사용하는 것이 좋다. 본 발명에서 사용하기 바람직한 가교 유기 첨가제는 가교 폴리메틸메타크릴레이트, 가교 폴리스티렌 및 가교 폴리메틸메타크릴레이트와 폴리스티렌의 공중합체로 이루어진 군에서 선택되는 어느 하나 이상이다.In addition, since the temperature of the melt extrusion process is 260 ° C. or more during film production, the heat resistance of the organic additive should be maintained above that. In order to have heat resistance in this temperature condition range, it is preferable to use a crosslinked organic additive. Preferred crosslinking organic additives for use in the present invention are any one or more selected from the group consisting of crosslinked polymethylmethacrylate, crosslinked polystyrene and copolymers of crosslinked polymethylmethacrylate and polystyrene.
그리고, 상술한 바와 같은 유기입자의 함량은 본 발명에 따른 폴리에스테르 필름 전체에 대하여 2 내지 15중량% 포함되는 것이 바람직한데, 그 이유는 2중량% 미만으로 포함되면 광확산 및 은폐력이 부족한 문제점이 있으며, 15중량%를 초과하여 포함되는 경우에는 과도한 은폐력으로 오히려 광확산 효과를 저하시킬 뿐만 아니라 필름의 제조 시 연신성이 불량해져 파단성이 증가하는 문제점이 발생하기 때 문이다.And, the content of the organic particles as described above is preferably included in the 2 to 15% by weight based on the entire polyester film according to the present invention, the reason is that when included in less than 2% by weight lack of light diffusion and hiding power In addition, when included in excess of 15% by weight, due to excessive hiding force, rather than lowering the light diffusion effect, as well as poor stretchability during the manufacture of the film is due to the problem that the breakage increases.
이러한 유기 첨가제 투입 방법으로는 다음 두가지 방식이 모두 가능하다.As such an organic additive input method, both of the following methods are possible.
첫 번째는, 유기 첨가제를 최종 필름에서의 필요 농도만큼 에틸렌글리콜로 슬러리화 하여 에스테르화 또는 에스테르 교환 반응이나 중축합 반응 중에 직접 투입하는 방법으로써 대량 생산에 유리한 방법이다. Firstly, the organic additives are slurried with ethylene glycol to the required concentration in the final film and directly added during esterification or transesterification or polycondensation, which is advantageous for mass production.
두 번째는, 컴파운딩에 의하여 유기 첨가제가 투입 되어있는 고농도의 마스터칩을 제조한 후, 압출 성형 공정에서 투입하는 방법으로써 이 경우 유기 첨가제의 손상 위험이 적고, 마스터 배치 칩의 희석 정도에 따라 첨가제의 투입 농도 조절이 용이하여 전술한 방법보다 바람직하다.The second method is to manufacture a high-density master chip into which an organic additive is added by compounding, and then add it in an extrusion process. In this case, there is little risk of damage to the organic additive, and the additive depends on the degree of dilution of the master batch chip. It is preferable to the above-mentioned method because the concentration of the is easily controlled.
이하, 본 발명에 따른 폴리에스테르 필름의 제조방법을 상세히 설명한다.Hereinafter, the manufacturing method of the polyester film according to the present invention will be described in detail.
먼저, 통상적인 방법에 의하여 제조된 상기 제1 및 제2 폴리에스테르 수지를 질소 분위기 하에서 각각 건조시킨다. 이어서, 상기 제1 폴리에스테르 수지 용융물을 압출하여 제1 필름층으로 하고, 이와 동시에 상기 제2 폴리에스테르 수지의 용융물을 상기 제1 필름층의 어느 하나의 면에서 형성하여 제2 필름층이 되도록 두 대의 압출기와 피더블럭이 장치된 티다이를 이용하여 공압출하여 2층으로 이루어진 미연신 필름을 제조한다. 이어서, 상기 미연신 필름을 총 연신비가 9배 이상이 되도록 이축 연신하고 열고정하면 본 발명에 따른 폴리에스테르 필름이 제조된다.First, the first and second polyester resins produced by conventional methods are respectively dried under a nitrogen atmosphere. Subsequently, the first polyester resin melt is extruded to form a first film layer, and at the same time, a melt of the second polyester resin is formed on either side of the first film layer to form a second film layer. Coextrusion is carried out using a T-die equipped with a large extruder and a feeder block to prepare an unstretched film composed of two layers. Subsequently, the biaxially stretched and heat-set the unstretched film so that the total draw ratio is 9 times or more to prepare a polyester film according to the present invention.
본 발명에 따른 폴리에스테르 필름의 총 연신비가 9배 이상이 되어야 하는 이유는 유기입자에 의해 보이드를 형성시킴으로써 적절한 은폐력을 유지하고 광확산 효과를 높이기 위한 점 때문이다.The total draw ratio of the polyester film according to the present invention should be 9 times or more because the voids are formed by the organic particles to maintain the proper hiding power and to enhance the light diffusion effect.
앞서 설명한 제조방법은 티다이법에 의한 압출을 중심으로 설명하였으나, 인플레이션법과 같이 본 발명이 속하는 기술분야에 널리 알려진 것이라면 특별한 제한 없이 이용 가능하다. 그리고, 본 발명에 따른 폴리에스테르 필름은 사용 용도에 따라 적절한 두께로 설계가 가능하고, 필요에 따라 표면에 다른 수지로 코팅 등에 의해 표면 처리하여 사용될 수 있다.The manufacturing method described above has been described mainly by extrusion by the Ti-die method, but can be used without particular limitation as long as it is well known in the art to which the present invention belongs, such as the inflation method. In addition, the polyester film according to the present invention may be designed to an appropriate thickness according to the intended use, and may be used by surface treatment by coating with another resin on the surface as necessary.
이하, 본 발명을 실시예를 통해 더욱 상세히 설명하고자 하는데, 본 발명의 범위가 하기 실시예로 한정되는 것이 아님은 물론이다. Hereinafter, the present invention will be described in more detail with reference to Examples, but the scope of the present invention is not limited to the following Examples.
본 발명의 실시예 및 비교예에 있어서, 제조된 필름의 각종 성능 평가는 다음의 측정 방법으로 실시하였다.In the Example and the comparative example of this invention, various performance evaluation of the produced film was performed with the following measuring method.
(1) 휘도 (1) luminance
탑콘(Topcon)제 BM7을 사용하여 측정하였다(Field 2o,거리 50cm). Measurement was made using Topcon BM7 (Field 2 o , distance 50 cm).
(2) 헤이즈 (2) haze
ASTM D1003의 방법에 의하여 측정하였다.It measured by the method of ASTM D1003.
(3) 빛투과율(3) light transmittance
ASTM D1003의 방법에 의하여 측정하였다.It measured by the method of ASTM D1003.
(4) 광확산층의 내마모성 평가(4) Evaluation of Wear Resistance of Light Diffusion Layer
광확산 층을 Tabor Abrasion Tester로써 100회 연마 후 무게 손실 양을 측정하여 평가하였다. The light diffusion layer was evaluated by measuring the weight loss amount after polishing 100 times with a Tabor Abrasion Tester.
(5) 평활도 측정 (5) smoothness measurement
필름의 컬, 웨이브 발생 양에 따라 3등급으로 평가하였으며, O는 양호, △는 보통 , X는 불량을 나타낸다. According to the curl and wave generation amount of the film was evaluated in three grades, O is good, △ is normal, X is poor.
<실시예 1> <Example 1>
디메틸테레프탈레이트와 에틸렌글리콜을 1:2 당량비로 혼합하고 에스테르 교환반응 촉매로 망간아세테이트를 0.03중량% 넣어 폴리에틸렌테레프탈레이트 단량체인 비스-히드록시에틸렌테레프탈레이트를 생성하고, 중합 촉매로서 산화안티몬을 0.05중량% 넣어 중축합 반응을 완결시켜 고유점도 0.640dl/g인 폴리에스테르 수지를 제조하였다. Dimethyl terephthalate and ethylene glycol were mixed in a 1: 2 equivalent ratio, 0.03% by weight of manganese acetate was used as a transesterification catalyst to produce bis-hydroxyethylene terephthalate, a polyethylene terephthalate monomer, and 0.05% of antimony oxide as a polymerization catalyst. % Of the polycondensation reaction was completed to prepare a polyester resin having an intrinsic viscosity of 0.640 dl / g.
제1 폴리에스테르 수지로는 별도의 첨가제를 넣지 않은 상기 폴리에스테르 수지를 100% 사용하였으며, 제2 폴리에스테르 수질로는 상기 폴리에스테르 수지 70w중량%에 평균 입경이 3㎛인 가교 폴리스티렌 입자가 30중량% 포함되어 있는 마스터 칩을 컴파운더 스큐류 rpm 300, 온도 270℃ 조건 하에서 제조한 후에 첨가제를 넣지 않은 폴리에스테르 수지와 1:1의 혼합비로 희석한 것을 사용하였다.As the first polyester resin, 100% of the polyester resin without any additives was used, and as the second polyester water quality, the weight of the crosslinked polystyrene particles having an average particle diameter of 3 μm and 70 wt% of the polyester resin was 30 weight. The prepared master chip was prepared under a compound skew rpm of 300 and a temperature of 270 ° C., and then diluted with a mixing ratio of 1: 1 with a polyester resin without an additive.
이어서, 두 대의 압출기와 피더블록이 장착된 티다이를 사용하여 상기 제1 폴리에스테르 수지를 제1 필름층으로 하고, 상기 제2 폴리에스테르 수지를 제2 필름층으로 하여 용융시킨 후 공압출하여 30℃로 냉각된 냉각롤에 밀착시켜 미연신 필름을 얻었다.Subsequently, the first polyester resin was used as a first film layer, the second polyester resin was used as a second film layer, and then co-extruded using a T-die equipped with two extruders and a feeder block. It contact | adhered to the cooling roll cooled with and obtained the unstretched film.
이렇게 하여 얻은 미연신 필름을 통상의 2축연신장치를 이용하여 종방향으로 3배, 횡방향으로 4배 연신시킨 후 200℃에서 열고정하여 2축 연신된 2층의 폴리에스테르 필름을 얻었다.The unstretched film thus obtained was stretched three times in the longitudinal direction and four times in the transverse direction using a conventional biaxial stretching apparatus, and then heat-set at 200 ° C. to obtain a biaxially stretched two-layer polyester film.
상기 폴리에스테르 필름을 주사현미경 사진으로 측정한 결과 상기 제1 필름 층의 두께는 100㎛였고, 제2 필름층의 두께는 20㎛이였다.The thickness of the said 1st film layer was 100 micrometers, and the thickness of the 2nd film layer was 20 micrometers when the said polyester film was measured with the scanning microscope photograph.
이렇게 얻은 필름의 헤이즈, 빛투과율, 휘도, 내마모성 및 평활도를 측정하여 표 1에 나타냈다. The haze, light transmittance, brightness, wear resistance and smoothness of the thus obtained film were measured and shown in Table 1.
<실시예 2> <Example 2>
실시예 1과 동일한 방법에 의하여 실시하되 제2 폴리에스테르에 첨가한 유기입자를 가교 폴리메틸메타크릴레이트로 하였다. The organic particles added to the second polyester as in Example 1 were used as the crosslinked polymethyl methacrylate.
<실시예 3> <Example 3>
실시예 1과 동일한 방법에 의하여 실시하되 제2 폴리에스테르에 평균입도가 0.3㎛인 폴리스티렌을 첨가하였다. A polystyrene having an average particle size of 0.3 μm was added to the second polyester in the same manner as in Example 1.
<실시예 4> <Example 4>
실시예 3과 동일한 방법에 의하여 실시하되 제2 폴리에스테르의 유기 입자 함량을 20중량%로 하고 필름의 총 연신비를 9배로 하였다. It carried out by the same method as Example 3, the organic particles content of the second polyester was 20% by weight and the total draw ratio of the film was 9 times.
<비교예 1> Comparative Example 1
실시예 1의 제1 폴리에스테르 단독으로 하는 100㎛의 폴리에스테르 필름을 제조하고 아크릴 수지 중에 15중량%의 가교 폴리스티렌을 포함하는 광확산 층을 코팅하여 필름을 완성하였다. A 100 micrometer polyester film made from the first polyester of Example 1 was prepared, and a light diffusion layer containing 15% by weight of crosslinked polystyrene in an acrylic resin was coated to complete the film.
<비교예 2>Comparative Example 2
비교예 1과 동일한 방법에 의하여 실시하되 코팅 층 중의 가교 폴리스티렌의 함량을 30중량%로 하였다. It carried out by the same method as the comparative example 1 but the content of the crosslinked polystyrene in the coating layer was 30% by weight.
<비교예 3>Comparative Example 3
실시예 1과 동일한 방법에 의하여 실시하되 제2 폴리에스테르에 평균입도가 0.1㎛인 폴리스티렌을 첨가하였다 A polystyrene having an average particle size of 0.1 μm was added to the second polyester in the same manner as in Example 1.
<비교예4> Comparative Example 4
실시예1과 동일한 방법으로 하되 필름의 연신비를 7.5로 하였다The draw ratio of the film was set to 7.5 in the same manner as in Example 1.
상기 표 1을 보면, 본 발명에 따른 폴리에스테르 필름인 실시예 1 내지 4의 필름은 헤이즈, 빛투광율, 휘도, 내마모성 및 평활도에서 코팅 방법을 따른 비교예 1과 2의 필름 및 본 발명의 범위를 벗어나는 비교예 3과 4의 필름에 비하여 매우 우수하다는 것을 알 수 있다.Referring to Table 1, the films of Examples 1 to 4, which are polyester films according to the present invention, show the films of Comparative Examples 1 and 2 according to the coating method in haze, light transmittance, brightness, wear resistance and smoothness, and the scope of the present invention. It turns out that it is very excellent compared with the film of the comparative examples 3 and 4 which deviate.
이상에서 살펴본 바와 같이, 본 발명은 평활성, 내구성, 가공성 등이 우수하며, 또한 제조 비용이 적게드는 광확산용 폴리에스테르 필름을 제공할 수 있다.As described above, the present invention can provide a polyester film for light diffusion that is excellent in smoothness, durability, processability, and the like, and also has low manufacturing cost.
Claims (9)
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KR1020000077406A KR100558841B1 (en) | 2000-12-16 | 2000-12-16 | Polyester films for diffusing light and manufacturing method of the same |
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KR1020000077406A KR100558841B1 (en) | 2000-12-16 | 2000-12-16 | Polyester films for diffusing light and manufacturing method of the same |
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KR20020048116A KR20020048116A (en) | 2002-06-22 |
KR100558841B1 true KR100558841B1 (en) | 2006-03-10 |
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KR1020000077406A KR100558841B1 (en) | 2000-12-16 | 2000-12-16 | Polyester films for diffusing light and manufacturing method of the same |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101084903B1 (en) | 2006-03-31 | 2011-11-17 | 도요 보세키 가부시키가이샤 | Light diffusion film |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100885608B1 (en) | 2006-05-30 | 2009-02-24 | 주식회사 엘지화학 | Multi-layered light diffusion plate and liquid crystal display device comprising the same |
KR101459165B1 (en) * | 2009-06-30 | 2014-11-10 | 코오롱인더스트리 주식회사 | Polyester film and manufacturing method of the same |
KR101998345B1 (en) * | 2012-09-28 | 2019-07-09 | 코오롱인더스트리 주식회사 | Manufacturing method of polyester |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0867808A (en) * | 1994-06-24 | 1996-03-12 | Toray Ind Inc | Polyester film for laminating metallic plate |
KR960021524A (en) * | 1994-12-19 | 1996-07-18 | 안시환 | Multilayer polyester film |
KR19990080116A (en) * | 1998-04-13 | 1999-11-05 | 장용균 | Polyester film and its manufacturing method |
KR20000060571A (en) * | 1999-03-17 | 2000-10-16 | 장용균 | Polyester film |
-
2000
- 2000-12-16 KR KR1020000077406A patent/KR100558841B1/en not_active IP Right Cessation
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0867808A (en) * | 1994-06-24 | 1996-03-12 | Toray Ind Inc | Polyester film for laminating metallic plate |
KR960021524A (en) * | 1994-12-19 | 1996-07-18 | 안시환 | Multilayer polyester film |
KR19990080116A (en) * | 1998-04-13 | 1999-11-05 | 장용균 | Polyester film and its manufacturing method |
KR20000060571A (en) * | 1999-03-17 | 2000-10-16 | 장용균 | Polyester film |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101084903B1 (en) | 2006-03-31 | 2011-11-17 | 도요 보세키 가부시키가이샤 | Light diffusion film |
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KR20020048116A (en) | 2002-06-22 |
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