WO2011111461A1 - 透明性積層シートの製造方法およびその透明性積層シート - Google Patents

透明性積層シートの製造方法およびその透明性積層シート Download PDF

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Publication number
WO2011111461A1
WO2011111461A1 PCT/JP2011/052747 JP2011052747W WO2011111461A1 WO 2011111461 A1 WO2011111461 A1 WO 2011111461A1 JP 2011052747 W JP2011052747 W JP 2011052747W WO 2011111461 A1 WO2011111461 A1 WO 2011111461A1
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Prior art keywords
base material
crystalline resin
material layer
sheet
resin
Prior art date
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Ceased
Application number
PCT/JP2011/052747
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English (en)
French (fr)
Japanese (ja)
Inventor
船木 章
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Idemitsu Unitech Co Ltd
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Idemitsu Unitech Co Ltd
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Application filed by Idemitsu Unitech Co Ltd filed Critical Idemitsu Unitech Co Ltd
Priority to CN201180013030.0A priority Critical patent/CN102791479B/zh
Priority to EP11753123.6A priority patent/EP2546056A4/en
Priority to US13/634,415 priority patent/US20130004783A1/en
Publication of WO2011111461A1 publication Critical patent/WO2011111461A1/ja
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/06Layered 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
    • B32B27/08Layered 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
    • 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
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/32Layered products comprising a layer of synthetic resin comprising polyolefins
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B7/00Layered products characterised by the relation between layers; Layered products characterised by the relative orientation of features between layers, or by the relative values of a measurable parameter between layers, i.e. products comprising layers having different physical, chemical or physicochemical properties; Layered products characterised by the interconnection of layers
    • B32B7/02Physical, chemical or physicochemical properties
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B7/00Layered products characterised by the relation between layers; Layered products characterised by the relative orientation of features between layers, or by the relative values of a measurable parameter between layers, i.e. products comprising layers having different physical, chemical or physicochemical properties; Layered products characterised by the interconnection of layers
    • B32B7/02Physical, chemical or physicochemical properties
    • B32B7/022Mechanical properties
    • 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 drums
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2250/00Layers arrangement
    • B32B2250/24All layers being polymeric
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2307/00Properties of the layers or laminate
    • B32B2307/40Properties of the layers or laminate having particular optical properties
    • B32B2307/412Transparent
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2307/00Properties of the layers or laminate
    • B32B2307/70Other properties
    • B32B2307/704Crystalline
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00Stock material or miscellaneous articles
    • Y10T428/31504Composite [nonstructural laminate]
    • Y10T428/31855Of addition polymer from unsaturated monomers
    • Y10T428/31909Next to second addition polymer from unsaturated monomers
    • Y10T428/31924Including polyene monomers

Definitions

  • the present invention relates to a method for producing a transparent laminated sheet and the transparent laminated sheet.
  • Crystalline resins typified by polypropylene are opaque due to their high crystallinity (crystallinity, crystallization speed, spherulite size, etc.) in ordinary film forming methods.
  • an additive formulation nucleating agent
  • Polymer design techniques such as suppression are taken.
  • As another means for expressing transparency there is a quenching method using a belt process as described in Patent Document 2. The film is applied in a film forming process in which polypropylene is sandwiched between a molten state and a belt and a roll kept at a low temperature and rapidly cooled.
  • a sheet that has undergone an extrusion film forming and quenching process by a belt process or a water cooling method as described in Patent Document 2 has many spherulites in the vicinity of the sheet surface, and the presence of these spherulites may reduce transparency. is there. Further, even when a specific linear low density polyethylene is added to polypropylene as described in Patent Document 3, further improvement in transparency is desired. Furthermore, in the configuration of Patent Document 3, since materials other than polypropylene must be added, the configuration is not a monomaterial, and it is difficult to recycle. Therefore, how to reduce the production of spherulites is a key point for further transparency. And by the present inventors' earnest study, it has been found that by controlling the stress applied during the extrusion of the resin, the crystal formed by the subsequent rapid cooling is changed. The present invention is born based on this new knowledge.
  • an object of the present invention is to provide a production method capable of improving the transparency of a transparent laminated sheet and the transparent laminated sheet.
  • a first base material layer formed of a crystalline resin and a second base material provided on at least one surface of the first base material layer and formed of a crystalline resin
  • a crystalline resin for forming the second base material layer having a melt flow rate higher than that of the crystalline resin for forming the first base material layer.
  • the MFR is large and the relaxation time is short
  • the crystalline resin for forming the first base material layer and the crystalline resin for forming the second base material layer are in a sheet state in a molten state. It is characterized in that it is extruded and rapidly cooled.
  • the first base material layer and the second base material layer have the same crystalline resin. Moreover, in this invention, it is preferable to set it as the structure which both said 1st base material layer and said 2nd base material layer are polypropylene resin.
  • the transparent laminated sheet of the present invention is characterized by being obtained by the method for producing a transparent laminated sheet described above.
  • a first base material layer formed of a crystalline resin
  • a second base material layer provided on at least one side of the first base material layer, and formed of a crystalline resin
  • the crystalline resin forming the second base material layer has a larger MFR and shorter relaxation time than the crystalline resin forming the first base material layer
  • the internal haze of the transparent laminated sheet provided with the second base material layer is 10% or more lower than the internal haze in the case of the first base material layer single layer.
  • the transparent laminated sheet has a first base material layer having a second base material layer formed of a crystalline resin provided on at least one surface thereof, and forms a second base material layer.
  • a second base material layer formed of a crystalline resin provided on at least one surface thereof, and forms a second base material layer.
  • the crystalline resin of the second base material layer can easily relieve the stress received on the sheet surface during extrusion, and as a result, crystal nucleation due to stress orientation can be suppressed.
  • the present invention since no nucleating agent is added, there is no fear that thermoforming is difficult because the crystallinity is increased and the range of thermoformability is narrowed. Therefore, in the method for producing a transparent laminated sheet of the present invention, transparency can be improved (haze reduction) as compared with the case where the first base material layer is extruded alone without adding a nucleating agent.
  • the manufacturing apparatus 1 shown in FIG. 1 includes an existing extruder such as a single-screw extruder or a multi-screw extruder (not shown), and a T-die 10 for forming a sheet is provided at the tip of the extruder. It has been.
  • the resin sheet 2 as a transparent lamination sheet has a laminated structure of 3 layers. Two types of polypropylene resins are used as the raw material resin.
  • the inner layer 2a as the first base material layer uses a polypropylene resin.
  • a polypropylene resin having a MFR larger than that of the inner layer 2a and a short relaxation time is used.
  • the outer layer 2b preferably has an MFR 1.5 times or more larger than that of the inner layer 2a. This is because if the MFR is less than 1.5 times, the effect of improving transparency is small.
  • the relaxation time is preferably 80% or less of the inner layer 2a. This is because if the relaxation time is greater than 80%, the effect of improving transparency is small.
  • the raw material resins for the inner layer 2a and the outer layer 2b may be prepared in pellet form.
  • the relaxation time ( ⁇ ) is the angular frequency when a frequency dispersion measurement is performed at a temperature of 175 ° C. with a cone plate of 25 mm ⁇ , a cone angle of 0.1 radians (rad) in a rotational rheometer manufactured by Rheometrics.
  • the relaxation time at ⁇ 0.01 rad / sec was determined.
  • the complex elastic modulus G * (i ⁇ ) measured for the resin pellet is defined as ⁇ * / ⁇ * by stress ⁇ * and strain ⁇ * as shown in the following formula (1), and the relaxation time ⁇ is It calculated
  • ⁇ ( ⁇ ) G '( ⁇ ) / ⁇ G "( ⁇ ) (2)
  • G ′ represents the storage elastic modulus
  • G ′′ represents the loss elastic modulus.
  • relaxation time ( ⁇ )
  • the relaxation time
  • the relaxation time is related to the ease of return of the molecular chain oriented in the extrusion direction during extrusion, and indicates that when the relaxation time is short, it returns easily.
  • the resin sheet 2 has three layers.
  • the resin sheet 2 is not limited to this, and may be two layers in which the outer layer 2b is formed on one side of the inner layer 2a, or may be four or more layers.
  • two types of polypropylene resins are used, the present invention is not limited to this, and three or more types of polypropylene resins may be used.
  • these pellets are thrown into the hopper of each extruder, and each is melt-kneaded. Thereafter, lamination is performed by a feed block method or a multi-manifold die method.
  • a coat hanger die and a slot die can be exemplified, and any die may be used as long as it can form a multilayer sheet.
  • first cooling roll 21 includes a first cooling roll 21, a second cooling roll 22, a third cooling roll 23, a fourth cooling roll 24, an endless belt 25, a cooling water spray nozzle 26, a water tank 27, and a water absorption roll. 28 and a peeling roll 29 are provided.
  • the surface of the first cooling roll 21 is covered with an elastic material 21a such as nitrile-butadiene rubber (NBR).
  • the elastic material 21a preferably has a hardness (measured by a method according to JIS K 6301A) of 80 degrees or less and a thickness of about 10 mm.
  • at least one of the first, third, and fourth cooling rolls 21, 23, and 24 has a rotation shaft connected to a rotation driving unit (not shown).
  • the second cooling roll 22 is a metal roll (mirror cooling roll) whose surface roughness (surface roughness: Rmax based on JIS B 0601 “Surface Roughness—Definition and Display”) is 0.3 ⁇ m or less.
  • a cooling means such as a water-cooling type (not shown) is incorporated therein.
  • Rmax surface roughness
  • Such a second cooling roll 22 sandwiches the inner layer 2a and the outer layer 2b melt-extruded from the T die 10 between the first cooling roll 21 via a metal endless belt 25 made of stainless steel or the like. Has been placed.
  • the endless belt 25 is a mirror surface having a surface roughness (Rmax) of 0.3 ⁇ m or less on the surface contacting the inner layer 2a and the outer layer 2b melt-extruded from the T-die 10, and the first, third and fourth cooling rolls. It is wound around 21, 23, 24 so as to be freely rotatable. At this time, the third and fourth cooling rolls 23 and 24 can be metal rolls, and the temperature of the endless belt 25 can be adjusted by incorporating a cooling means such as a water-cooling type (not shown) therein. Can be.
  • a cooling means such as a water-cooling type (not shown) therein. Can be.
  • the cooling water spray nozzle 26 is provided on the lower surface side of the second cooling roll 22, whereby the cooling water is sprayed on the back surface of the endless belt 25. In this way, by blowing cooling water from the cooling water spray nozzle 26, the endless belt 25 is rapidly cooled, and the inner layer 2a and the outer layer 2b, which are surface-welded by the first and second cooling rolls 21 and 22, are also rapidly cooled. be able to.
  • the water tank 27 is formed in a box shape whose upper surface is open, and is provided so as to cover the entire lower surface of the second cooling roll 22.
  • the water tank 27 collects cooling water sprayed on the back surface of the endless belt 25 and discharges the collected water from a discharge port 27 a formed on the lower surface of the water tank 27.
  • the water absorption roll 28 is installed on the side surface portion of the second cooling roll 22 on the third cooling roll 23 side so as to be in contact with the endless belt 25, and removes excess cooling water adhering to the back surface of the endless belt 25. belongs to.
  • the peeling roll 29 is disposed so as to guide the inner layer 2 a and the outer layer 2 b to the third cooling roll 23 and the endless belt 25, and the inner layer 2 a and the outer layer 2 b (resin sheet 2) after cooling are removed from the endless belt 25. It peels off.
  • the peeling roll 29 may be arranged so that the inner layer 2a and the outer layer 2b (resin sheet 2) are pressed against the third cooling roll 23 side, but are separated from the third cooling roll 23 as shown in the figure. It is preferable that the inner layer 2a and the outer layer 2b (resin sheet 2) are not pressed against each other.
  • the transparent polypropylene resin sheet is manufactured by the manufacturing apparatus configured as described above as follows.
  • the dew point is maintained at 50 ° C. or lower, preferably 30 ° C. or lower in advance. Temperature control of each cooling roll 22,23,24 is performed.
  • the surface temperature of the second cooling roll 22 and the endless belt 25 is equal to or lower than the dew point, condensation may occur on the surface, and uniform film formation may be difficult.
  • the surface temperature is higher than 50 ° C., the transparency of the resin sheet 2 to be obtained is lowered, the ⁇ crystal is increased, and there is a possibility that thermoforming is difficult.
  • the inner layer 2 a and the outer layer 2 b are melt-extruded from the T die 10 of the extruder, and sandwiched between the endless belt 25 and the second cooling roll 22 on the first cooling roll 21.
  • the inner layer 2a and the outer layer 2b are surface-welded with the first and second cooling rolls 21 and 22 and rapidly cooled.
  • the elastic material 21a coated on the surface of the first cooling roll 21 is compressed and elastically deformed, but the inner layer 2a and the outer layer 2b are portions where the elastic material 21a is elastically deformed, that is, the first cooling.
  • the first and second cooling rolls 21 and 22 are brought into surface pressure contact.
  • the surface pressure at this time is preferably 0.1 to 20 MPa.
  • the inner layer 2a and the outer layer 2b sandwiched between the second cooling roll 22 and the endless belt 25 are, in the arc portion corresponding to the substantially lower half circumference of the second cooling roll 22, the second cooling roll 22,
  • the sheet is pressed by the endless belt 25 and further cooled rapidly by cooling water sprayed onto the back side of the endless belt 25 by the cooling water spray nozzle 26.
  • the surface pressure at this time is preferably 0.01 to 0.5 MPa, and the temperature of the cooling water is preferably 0 to 30 ° C.
  • the sprayed cooling water is collected in the water tank 27, and the collected water is discharged from the drain port 27a.
  • the inner layer 2a and the outer layer 2b that are in close contact with the endless belt 25 after the surface cooling and cooling between the second cooling roll 22 and the endless belt 25 are performed on the inner layer 2a and the outer layer 2b.
  • the inner layer 2 a and the outer layer 2 b guided by the peeling roll 29 are rapidly cooled at an arc portion corresponding to the substantially upper half circumference of the third cooling roll 23.
  • the water adhering to the back surface of the endless belt 25 is removed by a water absorption roll 28 provided during the movement from the second cooling roll 22 to the third cooling roll 23.
  • the inner layer 2a and the outer layer 2b cooled on the third cooling roll 23, that is, the resin sheet 2 formed by rapidly cooling the inner layer 2a and the outer layer 2b are peeled from the endless belt 25 by the peeling roll 29, and are wound by a winding roll (not shown). It is wound at a predetermined speed.
  • the three-layer resin sheet 2 having the inner layer 2a and the outer layer 2b formed on both surfaces thereof is obtained.
  • the total thickness of the resin sheet 2 is 160 ⁇ m or more and less than 500 ⁇ m. This is because when the total thickness of the resin sheet 2 is less than 160 ⁇ m, there is sufficient quenching effect by each of the cooling rolls 21, 22, 23, 24, and transparency can be obtained to the extent that there is no need to laminate. . Furthermore, when the total thickness of the resin sheet 2 is 500 ⁇ m or more, a rapid cooling effect due to heat conduction cannot be expected, and as a result, a lamination effect cannot be exhibited.
  • the resin sheet 2 has outer layers 2b formed on both surfaces of the inner layer 2a, and the polypropylene resin forming the outer layer 2b has a larger MFR than the polypropylene resin forming the inner layer 2a.
  • the relaxation time is short.
  • the polypropylene resin of the outer layer 2b has a larger MFR and shorter relaxation time than the polypropylene resin of the inner layer 2a, so that the stress applied to the sheet surface during extrusion is easily relaxed, resulting in stress orientation. Crystal nucleation can be suppressed.
  • thermoforming becomes difficult. Therefore, in the method for producing the resin sheet 2 of the present embodiment, it is possible to improve transparency (reducing haze) without adding a nucleating agent.
  • the resin sheet 2 has a three-layer laminated structure, and two types of polypropylene resins are used as the raw material resin. For this reason, since the obtained resin sheet 2 becomes a monomaterial, it can be easily recycled.
  • the resin sheet 2 has an outer layer 2b of 30% or less of the total thickness of the resin sheet 2. For this reason, the influence of the haze by the outer layer 2b can be suppressed small, and the effect of a transparency improvement can be show
  • the total thickness of the resin sheet 2 is 160 ⁇ m or more and less than 500 ⁇ m. For this reason, there is sufficient quenching effect by each of the cooling rolls 21, 22, 23, 24 as in the case where the total thickness of the resin sheet 2 is less than 160 ⁇ m, and there is no need to dare to laminate or the total thickness of the resin sheet 2
  • the rapid cooling effect due to heat conduction cannot be expected as in the case where the thickness is 500 ⁇ m or more, and as a result, there is no fear that the effect of improving transparency cannot be achieved. Therefore, the effect of improving transparency can be effectively achieved.
  • the present invention is not limited to each of the above-described embodiments, and within the scope of achieving the objects and effects of the present invention.
  • Such modifications and improvements are included in the content of the present invention.
  • the same polypropylene resin is used as the crystalline resin of the inner layer 2a and the outer layer 2b, but the present invention is not limited to this. That is, a crystalline resin other than a polypropylene resin may be used, and it may not be a similar crystalline resin.
  • the cooling water is used for rapid cooling.
  • the present invention is not limited to this.
  • Examples 1 to 7 The specific conditions of the production apparatus and production method were as follows, and a resin sheet having a laminated structure was produced from the raw material resins shown in Table 1.
  • Table 2 shows the layer structure of the resin sheet, the total thickness of the layers, and the thickness of each layer in each example.
  • the relaxation time ( ⁇ ) is the angular frequency when a frequency dispersion measurement is performed at a temperature of 175 ° C. with a cone plate of 25 mm ⁇ , a cone angle of 0.1 radians (rad) in a rotational rheometer manufactured by Rheometrics.
  • the relaxation time at ⁇ 0.01 rad / sec was determined.
  • the complex elastic modulus G * (i ⁇ ) measured for the resin pellet is defined as ⁇ * / ⁇ * by stress ⁇ * and strain ⁇ * as shown in the following formula (1), and the relaxation time ⁇ is It calculated
  • ⁇ ( ⁇ ) G '( ⁇ ) / ⁇ G "( ⁇ ) (2)
  • G ′ represents the storage elastic modulus
  • G ′′ represents the loss elastic modulus.
  • Extruder dimensions, operating conditions, etc. are shown below.
  • Extruder ⁇ 90mm for the first base material layer, ⁇ 50mm for the second base material layer
  • Cooling roll and roll surface roughness Rmax 0.1 ⁇ m
  • Endless belt: Material precipitation hardening stainless steel, surface roughness Rmax 0.1 ⁇ m, width 900 mm, length 7700 mm, thickness 0.8 mm -Belt and mirror roll temperature of 16 ° C where melted sheet begins to contact ⁇
  • Table 2 shows the evaluation results.
  • the haze ratio can be reduced by 10% or more by laminating the resin sheet into two or more layers.
  • the resin sheet exhibits the effect of improving transparency when the total thickness is 160 ⁇ m to 500 ⁇ m.
  • the present invention can be applied to packaging uses such as foods, pharmaceuticals, and cosmetics.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Laminated Bodies (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)
PCT/JP2011/052747 2010-03-12 2011-02-09 透明性積層シートの製造方法およびその透明性積層シート Ceased WO2011111461A1 (ja)

Priority Applications (3)

Application Number Priority Date Filing Date Title
CN201180013030.0A CN102791479B (zh) 2010-03-12 2011-02-09 透明性积层片的制造方法以及其透明性积层片
EP11753123.6A EP2546056A4 (en) 2010-03-12 2011-02-09 METHOD FOR PRODUCING A TRANSPARENT COATED FILM AND TRANSPARENT COATED FOIL
US13/634,415 US20130004783A1 (en) 2010-03-12 2011-02-09 Method for manufacturing transparent laminated sheet, and transparent laminated sheet

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2010055493A JP5865577B2 (ja) 2010-03-12 2010-03-12 透明性積層シートの製造方法およびその透明性積層シート
JP2010-055493 2010-03-12

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US (1) US20130004783A1 (enExample)
EP (1) EP2546056A4 (enExample)
JP (1) JP5865577B2 (enExample)
CN (1) CN102791479B (enExample)
TW (1) TW201144068A (enExample)
WO (1) WO2011111461A1 (enExample)

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WO2012026478A1 (ja) * 2010-08-25 2012-03-01 出光ユニテック株式会社 透明性樹脂積層体の製造方法、成形体および樹脂積層体
JP2021053993A (ja) * 2019-09-25 2021-04-08 大日本印刷株式会社 積層体およびチューブ容器本体

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US20140264979A1 (en) * 2013-03-13 2014-09-18 Transitions Opticals, Inc. Method of preparing photochromic-dichroic films having reduced optical distortion
CN105291525B (zh) * 2015-09-17 2017-05-10 杭州中塑包装材料有限公司 与透析纸配合密封的抗高温卷曲易撕流延膜
CN108712954A (zh) * 2016-01-04 2018-10-26 格罗布兰股份有限公司 用于冷却薄膜材料的设备和方法
JP2020040258A (ja) * 2018-09-07 2020-03-19 大日本印刷株式会社 ガスバリア性積層体、包装材料用積層体および包装材料
JP2020157716A (ja) * 2019-03-28 2020-10-01 大日本印刷株式会社 基材、包装材料用積層体および包装材料
JP7725184B2 (ja) * 2018-09-07 2025-08-19 大日本印刷株式会社 包装材料用積層体および包装材料
JP2020040257A (ja) * 2018-09-07 2020-03-19 大日本印刷株式会社 積層基材、包装材料用積層体および包装材料
JP7491671B2 (ja) * 2019-05-27 2024-05-28 三井化学株式会社 積層体
JP2021000770A (ja) * 2019-06-21 2021-01-07 大日本印刷株式会社 保香性包装袋用積層体及び包装袋

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