WO2013038866A1 - Method for manufacturing film - Google Patents
Method for manufacturing film Download PDFInfo
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- 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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- WIPO (PCT)
- Prior art keywords
- film
- roll
- outer peripheral
- peripheral surface
- touch roll
- Prior art date
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- 238000004519 manufacturing process Methods 0.000 title claims abstract description 42
- 238000000034 method Methods 0.000 title abstract description 12
- 229920005989 resin Polymers 0.000 claims abstract description 21
- 239000011347 resin Substances 0.000 claims abstract description 21
- 230000003746 surface roughness Effects 0.000 claims abstract description 7
- 238000005266 casting Methods 0.000 claims description 39
- 230000002093 peripheral effect Effects 0.000 abstract description 48
- 230000000052 comparative effect Effects 0.000 description 40
- 229920005992 thermoplastic resin Polymers 0.000 description 16
- 238000011156 evaluation Methods 0.000 description 15
- 239000000155 melt Substances 0.000 description 7
- 230000015572 biosynthetic process Effects 0.000 description 6
- 238000001816 cooling Methods 0.000 description 5
- 238000003825 pressing Methods 0.000 description 4
- OCKGFTQIICXDQW-ZEQRLZLVSA-N 5-[(1r)-1-hydroxy-2-[4-[(2r)-2-hydroxy-2-(4-methyl-1-oxo-3h-2-benzofuran-5-yl)ethyl]piperazin-1-yl]ethyl]-4-methyl-3h-2-benzofuran-1-one Chemical compound C1=C2C(=O)OCC2=C(C)C([C@@H](O)CN2CCN(CC2)C[C@H](O)C2=CC=C3C(=O)OCC3=C2C)=C1 OCKGFTQIICXDQW-ZEQRLZLVSA-N 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 239000000853 adhesive Substances 0.000 description 2
- 230000001070 adhesive effect Effects 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 230000000996 additive effect Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000032798 delamination Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000004973 liquid crystal related substance Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 238000005498 polishing Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 238000013441 quality evaluation Methods 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 229920001169 thermoplastic Polymers 0.000 description 1
- 239000004416 thermosoftening plastic Substances 0.000 description 1
- 238000012795 verification Methods 0.000 description 1
Images
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C43/00—Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor
- B29C43/22—Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor of articles of indefinite length
- B29C43/222—Compression 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/03—Extrusion 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
- B29C48/07—Flat, e.g. panels
- B29C48/08—Flat, e.g. panels flexible, e.g. films
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/30—Extrusion nozzles or dies
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/30—Extrusion nozzles or dies
- B29C48/305—Extrusion nozzles or dies having a wide opening, e.g. for forming sheets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/362—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using static mixing devices
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/88—Thermal treatment of the stream of extruded material, e.g. cooling
- B29C48/91—Heating, e.g. for cross linking
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/88—Thermal treatment of the stream of extruded material, e.g. cooling
- B29C48/911—Cooling
- B29C48/9135—Cooling of flat articles, e.g. using specially adapted supporting means
- B29C48/915—Cooling of flat articles, e.g. using specially adapted supporting means with means for improving the adhesion to the supporting means
- B29C48/9155—Pressure rollers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/92—Measuring, controlling or regulating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92504—Controlled parameter
- B29C2948/92704—Temperature
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/88—Thermal treatment of the stream of extruded material, e.g. cooling
- B29C48/911—Cooling
- B29C48/9135—Cooling of flat articles, e.g. using specially adapted supporting means
- B29C48/914—Cooling 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
Description
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.
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
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
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
狭圧位置PAを通過後に流延膜FC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FCとの密着力が、TR外周面124と流延膜FC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FCとの密着力(あるいは、CR外周面126と流延膜FCとの密着力)そのものではなく、CR外周面126,流延膜FC間の密着力と、TR外周面124,流延膜FC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
(条件1)を、狭圧位置PA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PA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PA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
(Condition 2), the elastic of the CR outer
(Condition 3), the conditions used a temperature difference between the temperature (T TR) and the temperature of the CR outer
(Condition 4) is a condition using the film forming speed.
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.
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.
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.
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
FC 流延膜
PA 狭圧位置
PB 剥離位置
RAB 第1区間 100
Claims (2)
- 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、101≦ETR/ECR≦103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. - 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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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 |
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KR20140063680A (en) | 2014-05-27 |
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