WO2013038866A1 - Method for manufacturing film - Google Patents

Method for manufacturing film Download PDF

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Publication number
WO2013038866A1
WO2013038866A1 PCT/JP2012/070812 JP2012070812W WO2013038866A1 WO 2013038866 A1 WO2013038866 A1 WO 2013038866A1 JP 2012070812 W JP2012070812 W JP 2012070812W WO 2013038866 A1 WO2013038866 A1 WO 2013038866A1
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WO
WIPO (PCT)
Prior art keywords
film
roll
outer peripheral
peripheral surface
touch roll
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PCT/JP2012/070812
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French (fr)
Japanese (ja)
Inventor
達希 萩原
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コニカミノルタアドバンストレイヤー株式会社
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Priority to JP2013533578A priority Critical patent/JP5971253B2/en
Priority to KR1020147006320A priority patent/KR102014559B1/en
Publication of WO2013038866A1 publication Critical patent/WO2013038866A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C43/00Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor
    • B29C43/22Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor of articles of indefinite length
    • B29C43/222Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor of articles of indefinite length characterised by the shape of the surface
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • B29C48/07Flat, e.g. panels
    • B29C48/08Flat, e.g. panels flexible, e.g. films
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/30Extrusion nozzles or dies
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/30Extrusion nozzles or dies
    • B29C48/305Extrusion nozzles or dies having a wide opening, e.g. for forming sheets
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/362Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using static mixing devices
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/91Heating, e.g. for cross linking
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/911Cooling
    • B29C48/9135Cooling of flat articles, e.g. using specially adapted supporting means
    • B29C48/915Cooling of flat articles, e.g. using specially adapted supporting means with means for improving the adhesion to the supporting means
    • B29C48/9155Pressure rollers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/92Measuring, controlling or regulating
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92504Controlled parameter
    • B29C2948/92704Temperature
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/911Cooling
    • B29C48/9135Cooling of flat articles, e.g. using specially adapted supporting means
    • B29C48/914Cooling of flat articles, e.g. using specially adapted supporting means cooling drums

Definitions

  • the present invention relates to a film production method for producing a film by narrowing a molten resin between a touch roll and a cast roll.
  • thermoplastic resins thermoplastic resins
  • a highly productive film forming method such as a melt casting film forming method is known.
  • a molten resin containing a thermoplastic resin is extruded from the casting die onto the surface of the cast roll, and the extruded film shape.
  • Patent Documents 1 to 3 cannot cope with the improvement of the touch rolls alone when forming a film at high speed. That is, there is a problem of a peeling horizontal stage where a horizontal stage is formed in the molten resin when peeling from the cast roll, a problem of a horizontal stage where a horizontal stage is generated in the molten resin when the pressure is narrowed, and the molten resin is not partially in contact with the touch roll.
  • the problem of touch omission and the non-uniformity of the narrow pressure caused unevenness in the width direction such as the edges and the center, resulting in problems such as uneven pressing.
  • the present invention has been made in view of the above problems, stabilizes the uniformity of the narrow pressure by the touch roll and the cast roll, improves the peeling stability from the touch roll during high-speed film formation, and a film. It aims at providing the manufacturing method of the film which can obtain the flatness of this with high precision.
  • the method for producing a film according to the first aspect includes a step of narrowing the molten resin extruded from the casting die between the pressing portion of the touch roll and the pressing portion of the cast roll.
  • the surface roughness of the pressing portion in the touch roll is Ry TR
  • the surface roughness in the cast roll is Ry CR
  • the elasticity of the touch roll is E TR
  • the elasticity of the cast roll is When ECR is set, the relationship of 10 1 ⁇ E TR / E CR ⁇ 10 3 is satisfied.
  • the film manufacturing method according to the second aspect is the film manufacturing method according to the first aspect, wherein the surface temperature of the touch roll is TTR, and the surface temperature of the cast roll is TCR.
  • TTR surface temperature of the touch roll
  • TCR surface temperature of the cast roll
  • the manufacturing method of the film according to the first or second aspect by satisfying the relation of 1.5 ⁇ Ry TR / Ry CR, it is possible to improve the peeling stability from the touch roll. Moreover, the uniformity of the narrow pressure by a touch roll and a cast roll can be stabilized by satisfy
  • filling the relationship of 10 ⁇ 1 > ⁇ ETR / ECR . Furthermore, by satisfying the relationship of Ry TR ⁇ 0.2S, Ry TR / Ry CR ⁇ 4.0, and E TR / E CR ⁇ 10 3 , it becomes possible to obtain the flatness of the film with high accuracy. . As a result, a high quality film can be manufactured.
  • the uniformity of the narrow pressure between the touch roll and the cast roll can be further stabilized by satisfying the relationship of (T CR -T TR ) ⁇ 100 ° C. It becomes possible. Further, by satisfying the relationship of 1 ° C. ⁇ (T CR ⁇ T TR ), it is possible to further improve the peeling stability from the touch roll even during high-speed film formation. As a result, a higher quality film can be produced.
  • FIG. 1 is a schematic view showing a film manufacturing apparatus according to an embodiment of the present invention.
  • thermoplastic resin melt is used as a raw material for producing the film.
  • the thermoplastic resin melt is a viscous fluid in which additives necessary for the thermoplastic resin melt are mixed.
  • resin pellets and powdery resin compounds are used as raw materials for various thermoplastic melts.
  • FIG. 1 is a schematic diagram of a film manufacturing apparatus 100 according to the embodiment.
  • the film is manufactured using the melt casting film forming method.
  • a film manufacturing apparatus 100 shown in FIG. 1 includes a cast roll (first cooling roll) 102, a touch roll 104, a second cooling roll 106, a third cooling roll 108, a peeling roll 110, a longitudinal stretching preheating roll 18, and a longitudinal stretching machine 112a. , A transverse stretching machine 112b, a winder 114, a casting die 116, an extruder 118, and a control unit 160.
  • the resin is melted at 200 to 300 ° C. in the extruder 150, the melt of the resin is filtered by a leaf disk type filter 152, and in the static mixer 154, the resin in the resin at the tube wall and the tube center.
  • the resin components are made uniform. Thereby, a thermoplastic resin melt is generated, and the thermoplastic resin melt is sent from the extruder 118 to the casting die 116.
  • the required additive which concerns on this embodiment is previously mixed with resin before putting into the extruder 150.
  • the casting die 116 is close to and faces the outer peripheral surface of the cast roll 102 (hereinafter referred to as the CR outer peripheral surface 126).
  • the cast roll 102 rotates and the CR outer peripheral surface 126 travels in the vicinity of the casting die 116.
  • the liquid (thermoplastic resin melt) in which the thermoplastic resin is melted is supplied from the extruder 118 to the casting die 116, so that the thermoplastic resin melt is transferred from the casting die 116 to the CR outer peripheral surface 126.
  • a cast film F C (molten resin) of the thermoplastic resin melt is formed by being cast and narrowed by the roll outer surface (hereinafter referred to as TR outer peripheral surface 124) of the touch roll 104 and the CR outer peripheral surface 126. Is done.
  • Sema ⁇ position P A, of the TR outer peripheral surface 124 is a position where the thermoplastic resin melt which is cast by the casting die 116 is pressurized narrow at a cast roll 102 and the touch roll 104, a release position P B is the position where the casting film F C is peeled off from the CR outer peripheral surface 126.
  • Casting film F C is cooled and solidified in CR outer peripheral surface 126, it is peeled off from the CR outer peripheral surface 126.
  • Casting film F C peeled from CR outer peripheral surface 126 is subjected to pass to the second cooling roller 106 and the third cooling roller 108 traveling along the traveling path which meanders in a zigzag, longitudinal stretching through the longitudinal stretching pre-heating roll 18 It is led to the machine 112a, where it is stretched in the longitudinal direction (longitudinal direction).
  • casting film F C and where it is stretched in the transverse direction (width direction) is wound by a winder 114.
  • a roll of the film F OP is produced.
  • the control unit 160 includes a hardware configuration such as a storage unit and a CPU, and implements various functions by executing a program in the storage unit on the CPU or the like, for example. Specifically, the control unit 160 controls the operation timing of each component including the extruder 118 and the cast roll 102. Accordingly, the timing of each operation including the supply of the thermoplastic resin melt from the extruder 118 to the casting die 116 and the rotation of the cast roll 102 (CR outer peripheral surface 126) and the touch roll 104 (TR outer peripheral surface 124) is appropriately determined. Be controlled.
  • the roughness can be adjusted by changing the abrasive in the final polishing of each surface of the TR outer peripheral surface 124 and the CR outer peripheral surface 126 according to the target roughness.
  • the means for adjusting the elasticity the TR outer peripheral surface 124 and the CR outer peripheral surface 126 are adjusted by the material and surface processing method, or the TR outer peripheral surface 124 and the CR outer peripheral surface 126 are constituted by thin metal outer cylinder rolls. If it is, adjustment can be performed by the thickness of the outer cylinder.
  • the temperature adjusting means for the TR outer peripheral surface 124 and the CR outer peripheral surface 126 is adjusted by a temperature adjusting device including a heater or the like.
  • the manufacturing conditions according to the present embodiment are classified into the following four categories. That is, (Condition 1), the roughness of the TR outer peripheral surface 124 in Sema ⁇ position P A (Ry TR), the roughness of the CR outer peripheral surface 126 (Ry CR), and, the TR roughness Ry TR for CR roughness Ry CR A condition using the ratio (Ry TR / Ry CR ); (Condition 2), the elastic of the CR outer peripheral surface 126 in Sema ⁇ position P A (E CR) 1 and elasticity of the TR outer peripheral surface 124 when the representation ratio (E TR) (E TR / E CR) As a condition using (Condition 3), the conditions used a temperature difference between the temperature (T TR) and the temperature of the CR outer peripheral surface 126 (T CR) of TR outer peripheral surface 124 in Sema ⁇ position P A of (T CR -T TR); (Condition 4) is a condition using the film forming speed.
  • case study A as shown in Table 1 below, (Condition 1) and (Condition 2) were changed.
  • (Condition 3) and (Condition 4) were performed in a constant manner in any of Examples 1A to 4A and Comparative Examples 1A to 6A in Table 1 below.
  • the temperature (T TR ) of the TR outer peripheral surface 124 is 70 ° C.
  • the temperature (T CR ) of the CR outer peripheral surface 126 is 120 ° C.
  • the temperature difference (T CR ⁇ T TR ) is The test was carried out at a constant temperature of 50 ° C., and at a film forming speed of (Condition 4) of 10 m / min.
  • Example and Comparative Example in Case Study (Experiment) B> The produced film F OP in the following case studies B, referred to as Example 1B ⁇ 6B and Comparative Examples 1B ⁇ 6B.
  • Case Study B (Condition 4) and (Condition 3) were changed as shown in Table 3 below.
  • the film forming speed under condition 4 was 20 m / min (high-speed film formation) in each production of Examples 1B to 3B and Comparative Examples 1B to 3B, and 10 m / min in each production of Examples 4B to 6B and Comparative Examples 4B to 6B. It was minutes.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Shaping Of Tube Ends By Bending Or Straightening (AREA)

Abstract

A method for manufacturing a film, wherein a molten resin is pinched between a TR external peripheral face (124) and a CR external peripheral face (126) while the relationships RyTR ≤ 0.2S, RyCR ≤ 0.2S, and 1.5 ≤ RyTR/RyCR ≤ 4.0 are satisfied, the relationship 101 ≤ ETR/ECR ≤ 103 is satisfied, and the relationship 1°C ≤ (TCR - TTR) ≤ 100°C is satisfied, where RyTR is the surface roughness, ETR is the elasticity, and TTR is the temperature of the TR external peripheral face (124) of a touch roll (104), and RyCR is the surface roughness, ECR is the elasticity, and TCR is the temperature of the CR external peripheral face (126) of a cast roll (102). The uniformity of pinching by the touch roll and the cast roll can thereby be stabilized, the stability of peeling from the touch roll can be enhanced, and the film can be endowed with highly precise flatness.

Description

フィルムの製造方法Film production method
 本発明は、溶融樹脂をタッチロールとキャストロールとの間で狭圧してフィルムを製造するフィルムの製造方法に関する。 The present invention relates to a film production method for producing a film by narrowing a molten resin between a touch roll and a cast roll.
 近年、幅広く普及している液晶表示装置等では、熱可塑性を有する樹脂(熱可塑性樹脂)を用いたフィルムが利用されている。そして、熱可塑性樹脂を用いたフィルムの製膜方法としては、例えば、溶融流延製膜法等といった生産性の高い製膜方法が知られている。 In recent years, films using thermoplastic resins (thermoplastic resins) have been used in liquid crystal display devices and the like that are widely spread. As a film forming method using a thermoplastic resin, for example, a highly productive film forming method such as a melt casting film forming method is known.
 溶融流延成膜法によるフィルムの製造のうち代表的な製膜方法の一つとして、熱可塑性樹脂を含む溶融樹脂を流延ダイからキャストロールの表面にフィルム状に押し出し、押し出されたフィルム状の溶融樹脂をキャストロールとタッチロールとによって挟圧することによってフィルムを得る方法が挙げられる。この際、フィルムにかかる圧力が樹脂の配向状態に影響を与えるため、十分に均一な圧力で挟圧を行うことが重要になる。 As one of the typical film forming methods among films produced by the melt casting film forming method, a molten resin containing a thermoplastic resin is extruded from the casting die onto the surface of the cast roll, and the extruded film shape. A method of obtaining a film by sandwiching the molten resin with a cast roll and a touch roll. At this time, since the pressure applied to the film affects the orientation state of the resin, it is important to perform the clamping with a sufficiently uniform pressure.
 そこで、溶融樹脂を2本のロールで挟圧してフィルムを作製する方法において、残留歪みをなくし、幅手に均一に挟圧できるタッチロールの改良が行われてきた(例えば、特許文献1~3)。 Therefore, in a method for producing a film by sandwiching a molten resin with two rolls, improvement of a touch roll that eliminates residual distortion and can be uniformly sandwiched with a wide width has been performed (for example, Patent Documents 1 to 3). ).
特開平11-235747号公報Japanese Patent Laid-Open No. 11-235747 特開平2002-36332号公報Japanese Patent Laid-Open No. 2002-36332 特許第3422798号公報Japanese Patent No. 3422798
 しかしながら、上記特許文献1~3の技術では、高速で製膜する際にはそれらタッチロールの改良だけでは対応しきれなかった。すなわち、キャストロールからの剥離される時に溶融樹脂に横段が生じる剥離横段の問題、狭圧する時に溶融樹脂に横段が生じるキャスト横段の問題、タッチロールに溶融樹脂が部分的に接触しないタッチ抜けの問題、狭圧が均一でないために端や中央などの幅手方向でムラが生じる押圧ムラといった問題が生じてしまい、タッチロールのみの改良では片手落ちだった。 However, the techniques of Patent Documents 1 to 3 cannot cope with the improvement of the touch rolls alone when forming a film at high speed. That is, there is a problem of a peeling horizontal stage where a horizontal stage is formed in the molten resin when peeling from the cast roll, a problem of a horizontal stage where a horizontal stage is generated in the molten resin when the pressure is narrowed, and the molten resin is not partially in contact with the touch roll. The problem of touch omission and the non-uniformity of the narrow pressure caused unevenness in the width direction such as the edges and the center, resulting in problems such as uneven pressing.
 本発明は、上記課題に鑑みてなされたものであり、タッチロールとキャストロールとによる狭圧の均一性を安定化させ、高速製膜時のタッチロールからの剥離安定性を向上させるとともに、フィルムの平面性を高い精度で得ることが可能なフィルムの製造方法を提供することを目的とする。 The present invention has been made in view of the above problems, stabilizes the uniformity of the narrow pressure by the touch roll and the cast roll, improves the peeling stability from the touch roll during high-speed film formation, and a film. It aims at providing the manufacturing method of the film which can obtain the flatness of this with high precision.
 上記課題を解決するために、第1の態様に係るフィルムの製造方法は、流延ダイから押し出された溶融樹脂をタッチロールの挟圧部とキャストロールの挟圧部との間で狭圧する工程を含み、前記キャストロール側より前記溶融樹脂を送り出してフィルムを得る、フィルムの製造方法において、前記タッチロールにおける挟圧部の表面粗さをRyTRとし、前記キャストロールにおける表面粗さをRyCRとした場合に、RyTR≦0.2S、且つ、1.5≦RyTR/RyCR≦4.0の関係を満たし、前記タッチロールにおける弾性度をETRとし、前記キャストロールにおける弾性度をECRとした場合に、10≦ETR/ECR≦10の関係を満たすことを特徴とする。 In order to solve the above-mentioned problem, the method for producing a film according to the first aspect includes a step of narrowing the molten resin extruded from the casting die between the pressing portion of the touch roll and the pressing portion of the cast roll. In the method for producing a film, the surface roughness of the pressing portion in the touch roll is Ry TR, and the surface roughness in the cast roll is Ry CR And satisfying the relationship of Ry TR ≦ 0.2S and 1.5 ≦ Ry TR / Ry CR ≦ 4.0, the elasticity of the touch roll is E TR, and the elasticity of the cast roll is When ECR is set, the relationship of 10 1 ≦ E TR / E CR ≦ 10 3 is satisfied.
 また、第2の態様に係るフィルムの製造方法は、第1の態様に係るフィルムの製造方法であって、前記タッチロールにおける表面の温度をTTRとし、前記キャストロールにおける表面の温度をTCRとした場合に、1℃≦(TCR-TTR)≦100℃の関係を満たすことを特徴とする。 Moreover, the film manufacturing method according to the second aspect is the film manufacturing method according to the first aspect, wherein the surface temperature of the touch roll is TTR, and the surface temperature of the cast roll is TCR. In this case, the relationship of 1 ° C. ≦ (T CR −T TR ) ≦ 100 ° C. is satisfied.
 第1または第2の態様に係るフィルムの製造方法によれば、1.5≦RyTR/RyCRの関係を満たすことにより、タッチロールからの剥離安定性を向上させることが可能となる。また、10≦ETR/ECRの関係を満たすことにより、タッチロールとキャストロールとによる狭圧の均一性を安定化させることができる。さらに、RyTR≦0.2S、RyTR/RyCR≦4.0、および、ETR/ECR≦10の関係を満たすことにより、フィルムの平面性を高い精度で得ることが可能となる。その結果、高品質のフィルムを製造することができる。 According to the manufacturing method of the film according to the first or second aspect, by satisfying the relation of 1.5 ≦ Ry TR / Ry CR, it is possible to improve the peeling stability from the touch roll. Moreover, the uniformity of the narrow pressure by a touch roll and a cast roll can be stabilized by satisfy | filling the relationship of 10 < 1 ><= ETR / ECR . Furthermore, by satisfying the relationship of Ry TR ≦ 0.2S, Ry TR / Ry CR ≦ 4.0, and E TR / E CR ≦ 10 3 , it becomes possible to obtain the flatness of the film with high accuracy. . As a result, a high quality film can be manufactured.
 第2の態様に係るフィルムの製造方法によれば、(TCR-TTR)≦100℃の関係を満たすことにより、タッチロールとキャストロールとによる狭圧の均一性をより安定化させることが可能となる。また、1℃≦(TCR-TTR)の関係を満たすことにより、高速製膜時においてもタッチロールからの剥離安定性をより向上させることができる。その結果、より高品質なフィルムが製造することができる。 According to the film manufacturing method according to the second aspect, the uniformity of the narrow pressure between the touch roll and the cast roll can be further stabilized by satisfying the relationship of (T CR -T TR ) ≦ 100 ° C. It becomes possible. Further, by satisfying the relationship of 1 ° C. ≦ (T CR −T TR ), it is possible to further improve the peeling stability from the touch roll even during high-speed film formation. As a result, a higher quality film can be produced.
図1は本発明の実施形態に係るフィルム製造装置を示す模式図である。FIG. 1 is a schematic view showing a film manufacturing apparatus according to an embodiment of the present invention.
 以下、本発明の実施形態を図面に基づいて説明する。なお、図面は模式的に示されたものであり、構造のサイズおよび位置関係等は正確に図示されたものではない。 Hereinafter, embodiments of the present invention will be described with reference to the drawings. In addition, drawing is shown typically and the size of a structure, positional relationship, etc. are not illustrated correctly.
 <1.フィルム製造装置の概要>
 溶融流延製膜法を用いたフィルムの製造では、熱可塑性樹脂溶融液が、フィルムを製造するための原料として使用される。具体的には、熱可塑性樹脂溶融液は、熱可塑性樹脂の溶融物に必要な添加剤が混合されてなる粘性流体である。なお、熱可塑性種々の溶融物の原料としては、樹脂ペレットや紛体状の樹脂化合物が用いられる。
<1. Overview of film production equipment>
In the production of a film using the melt casting method, a thermoplastic resin melt is used as a raw material for producing the film. Specifically, the thermoplastic resin melt is a viscous fluid in which additives necessary for the thermoplastic resin melt are mixed. As raw materials for various thermoplastic melts, resin pellets and powdery resin compounds are used.
  <1-1.基本構成>
 図1は、実施形態に係るフィルム製造装置100の模式図である。フィルム製造装置100では、溶融流延製膜法を用いたフィルムの製造が行われる。
<1-1. Basic configuration>
FIG. 1 is a schematic diagram of a film manufacturing apparatus 100 according to the embodiment. In the film manufacturing apparatus 100, the film is manufactured using the melt casting film forming method.
 図1に示すフィルム製造装置100は、キャストロール(第1冷却ロール)102、タッチロール104、第2冷却ロール106、第3冷却ロール108、剥離ロール110、縦延伸予熱ロール18、縦延伸機112a、横延伸機112b、巻き取り機114、流延ダイ116、押出機118、および制御部160を備えている。 A film manufacturing apparatus 100 shown in FIG. 1 includes a cast roll (first cooling roll) 102, a touch roll 104, a second cooling roll 106, a third cooling roll 108, a peeling roll 110, a longitudinal stretching preheating roll 18, and a longitudinal stretching machine 112a. , A transverse stretching machine 112b, a winder 114, a casting die 116, an extruder 118, and a control unit 160.
 押出機118では、押出し機150において200~300℃で樹脂が溶融され、その樹脂の溶融物がリーフディスクタイプのフィルタ152でろ過され、スタチックミキサー154において管壁および管中央におけるその樹脂におけるその樹脂の成分を均一化している。これにより、熱可塑性樹脂溶融液が生成され、該熱可塑性樹脂溶融液が、押出機118から流延ダイ116へ送られる。なお、本実施形態に係る必要な添加剤は、押出し機150に入れる前の樹脂に予め混合されている。 In the extruder 118, the resin is melted at 200 to 300 ° C. in the extruder 150, the melt of the resin is filtered by a leaf disk type filter 152, and in the static mixer 154, the resin in the resin at the tube wall and the tube center. The resin components are made uniform. Thereby, a thermoplastic resin melt is generated, and the thermoplastic resin melt is sent from the extruder 118 to the casting die 116. In addition, the required additive which concerns on this embodiment is previously mixed with resin before putting into the extruder 150. FIG.
 流延ダイ116は、キャストロール102の外周面(以下、CR外周面126と称する)に近接し且つ対向する。 The casting die 116 is close to and faces the outer peripheral surface of the cast roll 102 (hereinafter referred to as the CR outer peripheral surface 126).
 フィルム製造装置100によりフィルムFOPが製造される際には、キャストロール102が回転し、CR外周面126が流延ダイ116の近傍を走行する。このとき、熱可塑性樹脂が溶融された液(熱可塑性樹脂溶融液)が押出機118から流延ダイ116へ供給されることで、流延ダイ116からCR外周面126へ熱可塑性樹脂溶融液が流延されてタッチロール104のロール外面(以下、TR外周面124と称する)とCR外周面126とにより狭圧されることにより熱可塑性樹脂溶融液の流延膜F(溶融樹脂)が形成される。CR外周面126のうち、狭圧位置PからCR外周面126の走行方向へ沿って剥離位置Pに至る迄の第1区間RABにおいて、熱可塑性樹脂溶融液の流延膜Fが形成される。なお、狭圧位置Pは、TR外周面124のうち、流延ダイ116によって流延された熱可塑性樹脂溶融液がキャストロール102とタッチロール104とで狭圧される位置であり、剥離位置Pは、流延膜FがCR外周面126から剥離される位置である。 When the film FOP is manufactured by the film manufacturing apparatus 100, the cast roll 102 rotates and the CR outer peripheral surface 126 travels in the vicinity of the casting die 116. At this time, the liquid (thermoplastic resin melt) in which the thermoplastic resin is melted is supplied from the extruder 118 to the casting die 116, so that the thermoplastic resin melt is transferred from the casting die 116 to the CR outer peripheral surface 126. A cast film F C (molten resin) of the thermoplastic resin melt is formed by being cast and narrowed by the roll outer surface (hereinafter referred to as TR outer peripheral surface 124) of the touch roll 104 and the CR outer peripheral surface 126. Is done. Of CR outer peripheral surface 126, the first section R AB from Sema圧position P A up to the stripping position P B along the running direction of the CR outer peripheral surface 126, the casting film F C of the thermoplastic resin melt is It is formed. Incidentally, Sema圧position P A, of the TR outer peripheral surface 124 is a position where the thermoplastic resin melt which is cast by the casting die 116 is pressurized narrow at a cast roll 102 and the touch roll 104, a release position P B is the position where the casting film F C is peeled off from the CR outer peripheral surface 126.
 流延膜Fは、CR外周面126で冷却および固化し、CR外周面126から剥離される。CR外周面126から剥離された流延膜Fは、第2冷却ロール106および第3冷却ロール108に渡しかけられてジグザグに蛇行する走行経路を走行し、縦延伸予熱ロール18を経て縦延伸機112aに導かれ、そこで縦方向(長手方向)に延伸される。続いて流延膜Fを横延伸機112bに導き、そこで横方向(幅方向)に延伸され、巻き取り機114で巻き取られる。これにより、フィルムFOPのロールが製造される。 Casting film F C is cooled and solidified in CR outer peripheral surface 126, it is peeled off from the CR outer peripheral surface 126. Casting film F C peeled from CR outer peripheral surface 126 is subjected to pass to the second cooling roller 106 and the third cooling roller 108 traveling along the traveling path which meanders in a zigzag, longitudinal stretching through the longitudinal stretching pre-heating roll 18 It is led to the machine 112a, where it is stretched in the longitudinal direction (longitudinal direction). Following lead to transverse stretching machine 112b casting film F C and where it is stretched in the transverse direction (width direction), is wound by a winder 114. Thus, a roll of the film F OP is produced.
  <1-2.動作の制御>
 フィルム製造装置100では、制御部160は、記憶部およびCPU等のハードウェア構成を含み、例えば、記憶部内のプログラムをCPU等において実行することにより、各種機能を実現する。具体的には、制御部160によって、押出機118と、キャストロール102とを含む各構成の動作タイミングを制御する。これにより、押出機118から流延ダイ116への熱可塑性樹脂溶融液の供給、キャストロール102(CR外周面126)およびタッチロール104(TR外周面124)の回転を含む各動作のタイミングが適宜制御される。
<1-2. Operation control>
In the film manufacturing apparatus 100, the control unit 160 includes a hardware configuration such as a storage unit and a CPU, and implements various functions by executing a program in the storage unit on the CPU or the like, for example. Specifically, the control unit 160 controls the operation timing of each component including the extruder 118 and the cast roll 102. Accordingly, the timing of each operation including the supply of the thermoplastic resin melt from the extruder 118 to the casting die 116 and the rotation of the cast roll 102 (CR outer peripheral surface 126) and the touch roll 104 (TR outer peripheral surface 124) is appropriately determined. Be controlled.
 <2.フィルムの製造方法>
 図1で示されたフィルム製造装置100がベースとされて、タッチロール104のTR外周面124およびキャストロール102のCR外周面126における、粗度(表面粗さ)、弾性度および温度が適宜変更されたフィルム製造装置を用いて、フィルムFOPが溶融流延製膜法によって製造される。
<2. Film production method>
Based on the film manufacturing apparatus 100 shown in FIG. 1, roughness (surface roughness), elasticity, and temperature on the TR outer peripheral surface 124 of the touch roll 104 and the CR outer peripheral surface 126 of the cast roll 102 are appropriately changed. The film FOP is manufactured by the melt casting film forming method using the prepared film manufacturing apparatus.
 ここで、粗度の調整手段として、TR外周面124およびCR外周面126の各表面の最終研磨における研磨剤を、目標粗度に合わせて変更することで粗度の調整を行える。また、弾性度の調整手段としては、TR外周面124およびCR外周面126の各表面の材質や表面加工方法による調整、あるいは、TR外周面124およびCR外周面126が薄肉金属外筒ロールから構成されていれば、外筒の肉厚で調整を行うことができる。さらに、TR外周面124およびCR外周面126の温度の調節手段としては、ヒータ等を含む温度調節装置等によって調整される。 Here, as a means for adjusting the roughness, the roughness can be adjusted by changing the abrasive in the final polishing of each surface of the TR outer peripheral surface 124 and the CR outer peripheral surface 126 according to the target roughness. Further, as the means for adjusting the elasticity, the TR outer peripheral surface 124 and the CR outer peripheral surface 126 are adjusted by the material and surface processing method, or the TR outer peripheral surface 124 and the CR outer peripheral surface 126 are constituted by thin metal outer cylinder rolls. If it is, adjustment can be performed by the thickness of the outer cylinder. Further, the temperature adjusting means for the TR outer peripheral surface 124 and the CR outer peripheral surface 126 is adjusted by a temperature adjusting device including a heater or the like.
  <2-1.実施例および比較例の製造条件>
 狭圧位置Pを通過後に流延膜FがTR外周面124から剥離する現象では、CR外周面126と流延膜Fとの密着力が、TR外周面124と流延膜Fとの密着力を上回れば剥離が安定する。すなわち、TR外周面124と流延膜Fとの密着力(あるいは、CR外周面126と流延膜Fとの密着力)そのものではなく、CR外周面126,流延膜F間の密着力と、TR外周面124,流延膜F間の密着力との差(比)が重要な意味を持つ。したがって、密着力に関しては、従来のタッチロール104単体の性能のみならず、対向するキャストロール102との性能のバランスこそが重要であり、2本のロールをトータルで考えた設計が必要となる。
<2-1. Production conditions of examples and comparative examples>
The phenomenon that after passing through the Sema圧position P A in the casting film F C is peeled off from the TR outer circumferential surface 124, adhesion between the CR outer peripheral surface 126 and the casting film F C is, TR outer peripheral surface 124 and the casting film F C Peeling becomes stable if the adhesive strength is exceeded. That is, the adhesion between the TR outer peripheral surface 124 and the casting film F C (or adhesive force between the CR outer peripheral surface 126 and the casting film F C) rather than itself, CR outer circumferential surface 126, between the casting film F C and adhesion, TR outer peripheral surface 124, the difference between the adhesion force between the casting film F C (ratio) has an important meaning. Therefore, regarding the adhesion, not only the performance of the conventional touch roll 104 alone but also the balance of the performance with the opposing cast roll 102 is important, and a design that considers the two rolls in total is required.
 そこで、本実施形態に係る製造条件として、下記4つのカテゴリに分類された。すなわち、
 (条件1)を、狭圧位置PにおけるTR外周面124の粗度(RyTR)、CR外周面126の粗度(RyCR)、および、CR粗度RyCRに対するTR粗度RyTRの比(RyTR/RyCR)を用いた条件とし;
 (条件2)を、狭圧位置PにおけるCR外周面126の弾性度(ECR)を1と表現したときのTR外周面124の弾性度(ETR)の比(ETR/ECR)を用いた条件とし;
 (条件3)を、狭圧位置PにおけるTR外周面124の温度(TTR)とCR外周面126の温度(TCR)との温度差(TCR-TTR)を用いた条件とし;
 (条件4)を、製膜速度を用いた条件とする。
Therefore, the manufacturing conditions according to the present embodiment are classified into the following four categories. That is,
(Condition 1), the roughness of the TR outer peripheral surface 124 in Sema圧position P A (Ry TR), the roughness of the CR outer peripheral surface 126 (Ry CR), and, the TR roughness Ry TR for CR roughness Ry CR A condition using the ratio (Ry TR / Ry CR );
(Condition 2), the elastic of the CR outer peripheral surface 126 in Sema圧position P A (E CR) 1 and elasticity of the TR outer peripheral surface 124 when the representation ratio (E TR) (E TR / E CR) As a condition using
(Condition 3), the conditions used a temperature difference between the temperature (T TR) and the temperature of the CR outer peripheral surface 126 (T CR) of TR outer peripheral surface 124 in Sema圧position P A of (T CR -T TR);
(Condition 4) is a condition using the film forming speed.
   <2-1-1.ケーススタディ(実験)Aにおける実施例および比較例>
 下記のケーススタディAにおいて製造されたフィルムFOPを、実施例1A~4Aおよび比較例1A~6Aと称する。ケーススタディAでは、下表1で示されるように、(条件1)および(条件2)が変更された。
<2-1-1. Example and Comparative Example in Case Study (Experiment) A>
The produced film F OP in the following case studies A, referred to as Examples 1A ~ 4A and Comparative Examples 1A ~ 6A. In case study A, as shown in Table 1 below, (Condition 1) and (Condition 2) were changed.
 また、下表2で示されるように、下表1における実施例1A~4Aおよび比較例1A~6Aのいずれの場合においても、(条件3) および(条件4)は一定で実施された。具体的には、(条件3)においては、TR外周面124の温度(TTR)が70℃、CR外周面126の温度(TCR)が120℃、温度差(TCR-TTR)が50℃で一定であり、且つ、(条件4)における製膜速度が10m/分の一定で実施された。 Further, as shown in Table 2 below, (Condition 3) and (Condition 4) were performed in a constant manner in any of Examples 1A to 4A and Comparative Examples 1A to 6A in Table 1 below. Specifically, in (Condition 3), the temperature (T TR ) of the TR outer peripheral surface 124 is 70 ° C., the temperature (T CR ) of the CR outer peripheral surface 126 is 120 ° C., and the temperature difference (T CR −T TR ) is The test was carried out at a constant temperature of 50 ° C., and at a film forming speed of (Condition 4) of 10 m / min.
Figure JPOXMLDOC01-appb-T000001
Figure JPOXMLDOC01-appb-T000001
Figure JPOXMLDOC01-appb-T000002
Figure JPOXMLDOC01-appb-T000002
 表1の具体的な条件として、条件1の粗度について、実施例1A~4Aおよび比較例3A,5A,6Aの各製造では、1.5≦RyTR/RyCR≦4.0の規定範囲内でRyTR、RyCRの値が変更された。また、比較例1A,2A,4Aの各製造では、1.5≦RyTR/RyCR≦4.0の規定範囲外に変更され、比較例1Aでは0.5、比較例2Aでは1、比較例4Aでは5とされた。また、比較例3Aの製造では、RyCRを0.25とし、残余の比較例および実施例1A~4Aでは、RyCR≦0.2Sとして実施された。さらに、比較例3A,4Aの製造では、RyTRを0.50とし、残余の比較例および実施例1A~4Aでは、RyTR≦0.2Sとして実施された。 As specific conditions in Table 1, with respect to the roughness of condition 1, in each production of Examples 1A to 4A and Comparative Examples 3A, 5A, and 6A, a specified range of 1.5 ≦ Ry TR / Ry CR ≦ 4.0 The values of Ry TR and Ry CR were changed. In Comparative Example 1A, 2A, each preparation of 4A is, 1.5 ≦ Ry TR / Ry CR ≦ 4.0 is changed outside the specified range of, in Comparative Example 1A 0.5 Comparative Example 2A 1, comparative In Example 4A, it was set to 5. In the production of Comparative Example 3A, Ry CR was set to 0.25, and in the remaining Comparative Examples and Examples 1A to 4A, Ry CR was set to 0.2S. Furthermore, in the manufacture of Comparative Examples 3A and 4A, Ry TR was set to 0.50, and in the remaining Comparative Examples and Examples 1A to 4A, Ry TR was set to 0.2S.
 条件2の弾性度について、実施例1A~4Aおよび比較例1A~4Aの各製造では、10≦ETR/ECR≦10の規定範囲内でETR、ECRの値が変更された。また、比較例5A,6Aの各製造では、10≦ETR/ECR≦10の規定範囲外に変更され、比較例5Aでは10、比較例2Aでは10とされた。 Regarding the elasticity of Condition 2, in each production of Examples 1A to 4A and Comparative Examples 1A to 4A, the values of E TR and E CR were changed within the specified range of 10 1 ≦ E TR / E CR ≦ 10 3 . . In Comparative Example 5A, in each production of 6A, it is changed outside the specified range of 10 1 ≦ E TR / E CR ≦ 10 3, Comparative Example 5A 10 0, which is a comparative Example 2A in 10 4.
   <2-1-2.ケーススタディ(実験)Bにおける実施例および比較例>
 下記のケーススタディBにおいて製造されたフィルムFOPを、実施例1B~6Bおよび比較例1B~6Bと称する。ケーススタディBでは、下表3で示されるように、(条件4)、および、(条件3)が変更された。
<2-1-2. Example and Comparative Example in Case Study (Experiment) B>
The produced film F OP in the following case studies B, referred to as Example 1B ~ 6B and Comparative Examples 1B ~ 6B. In Case Study B, (Condition 4) and (Condition 3) were changed as shown in Table 3 below.
 また、下表4で示されるように、下表3における実施例1B~6Bおよび比較例1B~6Bのいずれの場合においても、(条件1) および(条件2)は一定で実施された。具体的には、(条件1)においては、RyTRを0.10、RyCRを0.15、RyTR/RyCRを1.5の一定とし、(条件2)においては、ETR/ECRを10の一定とした。 Further, as shown in Table 4 below, (Condition 1) and (Condition 2) were carried out in a constant manner in any of Examples 1B to 6B and Comparative Examples 1B to 6B in Table 3 below. Specifically, in (Condition 1), Ry TR is 0.10, Ry CR is 0.15, and Ry TR / Ry CR is constant at 1.5, and in (Condition 2), E TR / E CR was defined as 10 1 constant.
Figure JPOXMLDOC01-appb-T000003
Figure JPOXMLDOC01-appb-T000003
Figure JPOXMLDOC01-appb-T000004
Figure JPOXMLDOC01-appb-T000004
 表3の具体的な条件として、条件3の温度について、実施例1B~6Bの各製造では、1℃≦(TCR-TTR)≦100℃の規定範囲内でTTR、TCRの値が変更された。また、比較例1B~6Bの各製造では、1℃≦(TCR-TTR)≦100℃の規定範囲外に変更され、比較例1B,4Bでは-120℃、比較例2B,5Bでは0℃、比較例3B,6Bでは20℃とされた。 As specific conditions in Table 3, with respect to the temperature of Condition 3, in the production of Examples 1B to 6B, the values of T TR and T CR are within the specified range of 1 ° C. ≦ (T CR −T TR ) ≦ 100 ° C. Has been changed. Further, in each production of Comparative Examples 1B to 6B, the temperature was changed outside the specified range of 1 ° C. ≦ (T CR −T TR ) ≦ 100 ° C., −120 ° C. in Comparative Examples 1B and 4B, and 0 in Comparative Examples 2B and 5B. The temperature was 20 ° C. in Comparative Examples 3B and 6B.
 条件4の製膜速度について、実施例1B~3Bおよび比較例1B~3Bの各製造では20m/分(高速成膜)とし、実施例4B~6Bおよび比較例4B~6Bの各製造では10m/分とされた。 The film forming speed under condition 4 was 20 m / min (high-speed film formation) in each production of Examples 1B to 3B and Comparative Examples 1B to 3B, and 10 m / min in each production of Examples 4B to 6B and Comparative Examples 4B to 6B. It was minutes.
  <2-2.本実施形態によるフィルムの性能検証>
 実施例1A~4Aと比較例1A~6Aとについて得られた製造結果が下表5に示され、実施例1B~6Bと比較例1B~6Bとについて得られた製造結果が下表6に示されている。
<2-2. Performance verification of film according to this embodiment>
The production results obtained for Examples 1A to 4A and Comparative Examples 1A to 6A are shown in Table 5 below, and the production results obtained for Examples 1B to 6B and Comparative Examples 1B to 6B are shown in Table 6 below. Has been.
 ここでは、下表5および下表6で示されるように、品質評価項目、および、評価レベル記載として、(評価1)TR外周面124からの流延膜Fの剥離安定性、(評価2)フィルムFOPの平面性、および、(評価3) キャストロール102とタッチロール104とによる狭圧均一性により評価された。 Here, as shown in the following table 5 and table 6, the quality evaluation items, and as a valuation described, (Evaluation 1) Peeling stability of the casting film F C from TR outer peripheral surface 124, (Evaluation 2 ) flatness of the film F OP, and was evaluated by (evaluation 3) narrow圧均one due the casting roll 102 and the touch roll 104.
 具体的には、(評価1)TR外周面124からの流延膜Fの剥離安定性に関して、フィルムFOPに対し45度の角度から点光源の光線を照射し、無地のスクリーンに投影した像を観察し、短手方向に横段状のムラが確認できなければ○(良判定)とし、確認できるが問題にならない弱いレベルならば△(許容範囲判定)とし、ムラが確認され製品として使用できないレベルであれば×(不良判定)とし、3段階で評価した。 Specifically, (Evaluation 1) with respect to delamination stability of the casting film F C from TR outer peripheral surface 124, is irradiated with light of a point light source at an angle of 45 degrees with respect to the film F OP, it is projected onto the plain screen Observe the image, if the horizontal unevenness in the short direction cannot be confirmed, ○ (good judgment), if it is a weak level that can be confirmed but does not cause a problem, △ (allowable range judgment), the unevenness is confirmed as a product If it was a level which cannot be used, it was set as x (defect determination) and evaluated in three steps.
 (評価2)フィルムFOPの平面性に関して、フィルムFOPに対し45度の角度から点光源の光線を照射し、無地のスクリーンに投影した像を観察し、長手方向にスジが確認できなければ○とし、確認できるが問題にならない弱いレベルなら△とし、スジがあり製品として使用できないレベルであれば×とし、3段階で評価した。 With respect to the plane of the (Evaluation 2) film F OP, irradiated with light of a point light source at an angle of 45 degrees with respect to the film F OP, to observe the image projected onto the plain screen, if confirmed stripes longitudinally The evaluation was made in three stages, with ◯, if it was a weak level that could be confirmed but not causing a problem, and △ if the level was streaky and could not be used as a product.
 (評価3) キャストロール102とタッチロール104とによる狭圧の均一性に関しては、フィルムFOPに対し正面から点光源の光線を照射し、無地のスクリーンに投影した像を観察し、長手方向3mにわたってタッチ抜け(局所的な未挟圧部分)の発生がなければ○とし、2個以下であれば△とし、3個以上であれば×とし、3段階で評価した。 (Evaluation 3) With respect to the narrow pressure uniformity due to the casting roll 102 and the touch roll 104, is irradiated with light of a point light source from the front to the film F OP, to observe the image projected onto the plain screen, longitudinal 3m When there was no occurrence of touch omission (local unclamped portion) over a range of ◯, the number was 2 or less, and the case of 3 or more was evaluated as x.
   <2-2-1.ケーススタディAに対する製造結果> <2-2-1. Manufacturing results for Case Study A>
Figure JPOXMLDOC01-appb-T000005
Figure JPOXMLDOC01-appb-T000005
 表5で示されるように、(評価1)TR外周面124からの流延膜Fの剥離安定性においては、実施例1A~4Aおよび比較例3A~6Aの何れについても、○であるのに対し、比較例1A,2Aに関しては、×という結果が得られた。このことから、タッチロール104(TR外周面124)からの流延膜Fの剥離安定性を良好にするためには、1.5≦RyTR/RyCRの関係を満たすことが必要であると確認された。 As shown in Table 5, (Evaluation 1) In the peel stability of the casting film F C from TR outer peripheral surface 124, for any of Examples 1A ~ 4A and Comparative Examples 3A ~ 6A, in the range of ○ On the other hand, as for Comparative Examples 1A and 2A, a result of x was obtained. Therefore, in order to improve the peel stability of the casting film F C from the touch roll 104 (TR outer circumferential surface 124), it is necessary to satisfy the relation of 1.5 ≦ Ry TR / Ry CR It was confirmed.
 (評価2) フィルムFOPの平面性においては、実施例1A~4Aおよび比較例1A,2A,5Aの何れについても、○であるのに対し、比較例3A,4A,6Aに関しては、×という結果が得られた。このことから、フィルムFOPの平面性を高い精度で得るためには、RyTR≦0.2S、RyCR≦0.2S、RyTR/RyCR≦4.0、および、ETR/ECR≦10の関係を満たすことが必要であると確認された。 (Evaluation 2) In the flatness of the film F OP, each of Examples 1A to 4A and Comparative Examples 1A, 2A, and 5A is ○, whereas Comparative Examples 3A, 4A, and 6A are indicated by ×. Results were obtained. From this, in order to obtain the flatness of the film F OP with high accuracy, Ry TR ≦ 0.2S, Ry CR ≦ 0.2S, Ry TR / Ry CR ≦ 4.0, and E TR / E CR It was confirmed that it was necessary to satisfy the relationship of ≦ 10 3 .
 (評価3) キャストロール102とタッチロール104とによる狭圧の均一性においては、実施例1A~4Aおよび比較例1A~4A,6Aの何れについても、○であるのに対し、比較例5Aに関しては、×という結果が得られた。このことから、キャストロール102とタッチロール104とによる狭圧の均一性を安定化させるためには、10≦ETR/ECRの関係を満たすことが必要であると確認された。 (Evaluation 3) In the uniformity of the narrow pressure between the cast roll 102 and the touch roll 104, each of Examples 1A to 4A and Comparative Examples 1A to 4A and 6A is ○, whereas Comparative Example 5A Resulted in x. From this, in order to stabilize the uniformity of the narrow pressure by the cast roll 102 and the touch roll 104, it was confirmed that it was necessary to satisfy the relationship of 10 1 ≦ E TR / E CR .
 以上の評価1~3により、RyTR≦0.2S、RyCR≦0.2S、1.5≦RyTR/RyCR≦4.0、および、10≦ETR/ECR≦10の関係を満たす場合、高品質のフィルムを製造することが可能と推察される。 From the above evaluations 1 to 3, Ry TR ≦ 0.2S, Ry CR ≦ 0.2S, 1.5 ≦ Ry TR / Ry CR ≦ 4.0, and 10 1 ≦ E TR / E CR ≦ 10 3 If the relationship is satisfied, it is assumed that a high-quality film can be produced.
   <2-2-2.ケーススタディBに対する製造結果> <2-2-2. Manufacturing results for Case Study B>
Figure JPOXMLDOC01-appb-T000006
Figure JPOXMLDOC01-appb-T000006
 表6で示されるように、(評価1)TR外周面124からの流延膜Fの剥離安定性においては、実施例1B~6Bおよび比較例1B、4B~6Bの何れについても、○であるのに対し、比較例2B,3Bに関しては、△という結果が得られた。このことから、タッチロール104(TR外周面124)からの流延膜Fの剥離安定性をより良好にするためには、20m/分程度の高速製膜時においては、とりわけ、1℃≦(TCR-TTR)の関係を満たすことが必要であると確認された。 As shown in Table 6, (Evaluation 1) In the peel stability of the casting film F C from TR outer peripheral surface 124, Example 1B ~ 6B and Comparative Examples 1B, for any of the 4B ~ 6B, with ○ On the other hand, the results of Δ were obtained for Comparative Examples 2B and 3B. Therefore, in order to better the release stability of the casting film F C from the touch roll 104 (TR outer circumferential surface 124), at the time of high-speed film of about 20 m / min, especially, 1 ° C. ≦ It was confirmed that it was necessary to satisfy the relationship (T CR -T TR ).
 (評価2) フィルムFOPの平面性においては、実施例1B~6Bおよび比較例4B~6Bの何れについても、○であるのに対し、比較例1B~3Bに関しては、△という結果が得られた。このことから、フィルムFOPの平面性をより高い精度で得るためには、20m/分程度の高速製膜時においては、とりわけ、1℃≦(TCR-TTR)≦100℃の関係を満たすことが必要であると確認された。 (Evaluation 2) With respect to the flatness of the film F OP, each of Examples 1B to 6B and Comparative Examples 4B to 6B is ○, whereas Comparative Example 1B to 3B has a result of Δ. It was. From this, in order to obtain the flatness of the film F OP with higher accuracy, the relationship of 1 ° C. ≦ (T CR −T TR ) ≦ 100 ° C. is particularly required at the time of high-speed film formation of about 20 m / min. It was confirmed that it was necessary to meet.
 (評価3) キャストロール102とタッチロール104とによる狭圧の均一性においては、実施例1B~6Bおよび比較例2B~6Bの何れについても、○であるのに対し、比較例1Bに関しては、△という結果が得られた。このことから、キャストロール102とタッチロール104とによる狭圧の均一性をより安定化させるためには、20m/分程度の高速製膜時においては、とりわけ、(TCR-TTR)≦100℃の関係を満たすことが必要であると確認された。 (Evaluation 3) In the uniformity of the narrow pressure between the cast roll 102 and the touch roll 104, all of Examples 1B to 6B and Comparative Examples 2B to 6B are ◯, whereas for Comparative Example 1B, A result of Δ was obtained. From this, in order to further stabilize the uniformity of the narrow pressure between the cast roll 102 and the touch roll 104, (T CR -T TR ) ≦ 100, especially at the time of high-speed film formation of about 20 m / min. It was confirmed that it was necessary to satisfy the relationship of ° C.
 以上の評価1~3により、20m/分程度の高速製膜時においては、RyTR≦0.2S、RyCR≦0.2S、1.5≦RyTR/RyCR≦4.0、および、10≦ETR/ECR≦10の関係を満たした上で、さらに、1℃≦(TCR-TTR)≦100℃の関係を満たす場合に、より高品質のフィルムを製造することが可能と推察される。 From the above evaluations 1 to 3, Ry TR ≦ 0.2S, Ry CR ≦ 0.2S, 1.5 ≦ Ry TR / Ry CR ≦ 4.0, and at the time of high-speed film formation of about 20 m / min, and A film of higher quality is manufactured when the relationship of 1 ° C. ≦ (T CR −T TR ) ≦ 100 ° C. is satisfied while satisfying the relationship of 10 1 ≦ E TR / E CR ≦ 10 3. It is assumed that this is possible.
 100 フィルム製造装置
 104 タッチロール
 124 TR外周面
 102 キャストロール
 126 CR外周面
 160 制御部
 118 押出機
 FOP フィルム
 F 流延膜
 P 狭圧位置
 P 剥離位置
 RAB 第1区間
100 film manufacturing apparatus 104 touch roll 124 TR outer peripheral surface 102 a cast roll 126 CR outer peripheral surface 160 controller 118 extruder F OP film F C casting film P A Sema圧position P B peeling position R AB first section

Claims (2)

  1.  流延ダイから押し出された溶融樹脂をタッチロールとキャストロールとの間で狭圧する工程を含み、前記キャストロール側より前記溶融樹脂を送り出してフィルムを得る、フィルムの製造方法において、
     前記タッチロールにおける表面粗さをRyTRとし、前記キャストロールにおける表面粗さをRyCRとした場合に、RyTR≦0.2S、RyCR≦0.2S、且つ、1.5≦RyTR/RyCR≦4.0の関係を満たし、
     前記タッチロールにおける弾性度をETRとし、前記キャストロールにおける弾性度をECRとした場合に、10≦ETR/ECR≦10の関係を満たすことを特徴とする、
    フィルムの製造方法。
    In the method for producing a film, including a step of narrowing a molten resin extruded from a casting die between a touch roll and a cast roll, and obtaining a film by feeding the molten resin from the cast roll side,
    When the surface roughness of the touch roll is Ry TR, and the surface roughness of the cast roll is Ry CR , Ry TR ≦ 0.2S, Ry CR ≦ 0.2S, and 1.5 ≦ Ry TR / Satisfies the relationship of Ry CR ≦ 4.0,
    The elasticity of the touch roll and E TR, when the elasticity of the E CR of the casting rolls, characterized by satisfying the relation of 10 1 ≦ E TR / E CR ≦ 10 3,
    A method for producing a film.
  2.  請求項1に記載のフィルムの製造方法であって、
     前記タッチロールにおける表面の温度をTTRとし、前記キャストロールにおける表面の温度をTCRとした場合に、1℃≦(TCR-TTR)≦100℃の関係を満たすことを特徴とする、
    フィルムの製造方法。
    It is a manufacturing method of the film of Claim 1, Comprising:
    Wherein the temperature of the surface and T TR of the touch roll, the temperature of the surface of the casting rolls when the T CR, and satisfies a 1 ℃ ≦ (T CR -T TR ) ≦ 100 ℃ relationship,
    A method for producing a film.
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018167456A (en) * 2017-03-29 2018-11-01 株式会社カネカ Method for producing film
US11638958B2 (en) 2014-03-11 2023-05-02 Tekna Plasma Systems Inc. Process and apparatus for producing powder particles by atomization of a feed material in the form of an elongated member

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004017305A (en) * 2002-06-12 2004-01-22 Tootsuya:Kk Method for surface working by film transferring system and film transferring surface working printed matter
JP2004330651A (en) * 2003-05-08 2004-11-25 Sekisui Chem Co Ltd Method for manufacturing optical film
JP2010234747A (en) * 2009-03-31 2010-10-21 Fujifilm Corp Film and method for manufacturing the same, optical compensation film for liquid crystal display panel, polarizing plate, and liquid crystal display device
JP2011173415A (en) * 2010-01-26 2011-09-08 Sumitomo Chemical Co Ltd Method of manufacturing surface protective film

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3422798B2 (en) 1996-02-09 2003-06-30 エス・エイチ・アイ モダンマシナリー株式会社 Roll for forming thin film sheet, sheet forming machine, and sheet forming method
JP3194904B2 (en) 1998-02-24 2001-08-06 日立造船株式会社 Roll equipment for sheet and film forming
JP2002036332A (en) 2000-07-24 2002-02-05 Toshiba Mach Co Ltd Molding roll for manufacturing thin film sheet
KR20090019808A (en) * 2006-05-31 2009-02-25 코니카 미놀타 옵토 인코포레이티드 Protective film for polarizer and process for producing the same, polarizer and process for producing the same, and liquid-crystal display
CN101801638A (en) * 2007-09-21 2010-08-11 住友化学株式会社 Process for producing optical film made of thermoplastic resin
JP2010076279A (en) * 2008-09-26 2010-04-08 Konica Minolta Opto Inc Manufacturing method of optical film, optical film, polarizing plate and liquid crystal display
KR101597854B1 (en) 2008-10-18 2016-02-25 코니카 미놀타 어드밴스드 레이어즈 인코포레이티드 Optical film for polarizing plate, method for producing same, polarizing plate using same and liquid crystal display device
JP2011143717A (en) * 2009-12-18 2011-07-28 Sumitomo Chemical Co Ltd Manufacturing method for sheet made of polypropylene resin

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004017305A (en) * 2002-06-12 2004-01-22 Tootsuya:Kk Method for surface working by film transferring system and film transferring surface working printed matter
JP2004330651A (en) * 2003-05-08 2004-11-25 Sekisui Chem Co Ltd Method for manufacturing optical film
JP2010234747A (en) * 2009-03-31 2010-10-21 Fujifilm Corp Film and method for manufacturing the same, optical compensation film for liquid crystal display panel, polarizing plate, and liquid crystal display device
JP2011173415A (en) * 2010-01-26 2011-09-08 Sumitomo Chemical Co Ltd Method of manufacturing surface protective film

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11638958B2 (en) 2014-03-11 2023-05-02 Tekna Plasma Systems Inc. Process and apparatus for producing powder particles by atomization of a feed material in the form of an elongated member
US11951549B2 (en) 2014-03-11 2024-04-09 Tekna Plasma Systems Inc. Process and apparatus for producing powder particles by atomization of a feed material in the form of an elongated member
JP2018167456A (en) * 2017-03-29 2018-11-01 株式会社カネカ Method for producing film

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