Biaxially stretched polyamide resin film
US-2015064485-A1 · Mar 5, 2015 · US
US10464253B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10464253-B2 |
| Application number | US-201515300527-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 26, 2015 |
| Priority date | Mar 31, 2014 |
| Publication date | Nov 5, 2019 |
| Grant date | Nov 5, 2019 |
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A method of manufacturing a biaxially stretched film according by: (I) preheating a thermoplastic resin film to a temperature in a rubbery plateau region in a storage elastic modulus curve; (II) biaxially stretching the thermoplastic resin film under a condition that a stretching speed is 500%/min or higher while heating the thermoplastic resin film to the temperature in the rubbery plateau region; (III) cooling the thermoplastic resin film after the biaxially stretching (II) to a temperature in a glass-to-rubber transition region or a glass region in the storage elastic modulus curve; and (IV) relaxing the thermoplastic resin film after the cooling (III) at a temperature in the glass-to-rubber transition region.
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The invention claimed is: 1. A method of manufacturing a biaxially stretched film in which an unstretched thermoplastic resin film comprising at least one thermoplastic resin layer is biaxially stretched in a longitudinal direction and a width direction to manufacture the biaxially stretched film, the method comprising: (I) preheating the thermoplastic resin film to a temperature in a rubbery plateau region in a storage elastic modulus curve; (II) biaxially stretching the thermoplastic resin film under a condition that a stretching speed is 500%/min or higher while heating the thermoplastic resin film to the temperature in the rubbery plateau region; (III) subsequently cooling the thermoplastic resin film to a temperature in a glass-to-rubber transition region or a glass region in the storage elastic modulus curve; and (IV) subsequently relaxing the thermoplastic resin film at a temperature in the glass-to-rubber transition region, wherein both a relaxation speed in the longitudinal direction and a relaxation speed in the width direction in said relaxing (IV) are 80%/min or higher, and wherein both a stretching magnification of the thermoplastic resin film in the longitudinal direction and a stretching magnification of the thermoplastic resin film in the width direction after (II) to (IV) with respect to the thermoplastic resin film before said biaxially stretching (II) are 1.5 to 3 times, wherein the at least one thermoplastic resin layer comprises a methacryl resin in which a triad syndiotacticity (rr) is 50% or larger. 2. The method according to claim 1 , wherein both a relaxation rate in the longitudinal direction and a relaxation rate in the width direction in said relaxing (IV) with respect to the thermoplastic resin film after said cooling (III) are 5 to 10. 3. The method according to claim 1 , wherein the biaxially stretched film has a deformation rate (%) expressed by the following Expression (1) of 0 to 0.5%: Deformation rate (%)=Δ L (mm)/10 (mm)×100 (1) wherein ΔL (mm)=L85 (mm)−L45 (mm), and wherein the deformation rate (%) is measured by: cutting a test piece with a length of 20 mm, a width of 5 mm, and a thickness of 45 μm out of the biaxially stretched film; holding both end parts of the test piece in the longitudinal direction by a pair of film chucks, setting a distance between the pair of film chucks to 10 mm; applying a pulling load of 2 g to the biaxially stretched film; attaching the test piece to a thermomechanical analyzer; heating the the test piece from 25° C. to 85° C. at a heating speed of 2° C./min, holding the temperature of the test piece at 85° C. for 30 minutes, and measuring a length of the test piece at 85° C., to obtain L85 (mm); and heating the test piece from 25° C. to 45° C. at a heating speed of 2° C./min and measuring a length of the test piece at 45° C., to obtain L45 (mm). 4. The method according to claim 1 , wherein the methacryl resin has a mass average molecular weight from 80,000 to 200,000, and a content of a monomer unit derived from methyl methacrylate of 92 mass % or more. 5. The method according to claim 1 , wherein the at least one thermoplastic resin layer comprises: methacryl resin (X), which is the methacryl resin; and carbonate resin (Y) in which a melt volume flow rate measured at 300° C., with a load of 1.2 kg, for 10 minutes is 130 to 250 cm3/10 min, wherein a mass ratio of the methacryl resin (X) to the carbonate resin (Y) is 91/9 to 99/1, and wherein a total amount of the methacryl resin (X) and the carbonate resin (Y) in the at least one thermoplastic resin layer is 80 to 100 mass %. 6. The method according to claim 1 , wherein the at least one thermoplastic resin layer comprises: methacryl resin (X), which is the methacryl resin; and phenoxy resin (Z), wherein an amount of the phenoxy resin (Z) with respect to 100 parts by mass of the methacryl resin (X) is 0.1 to 8 parts by mass, and wherein a total amount of the methacryl resin (X) and the phenoxy resin (Z) in the at least one thermoplastic resin layer is 80 to 100 mass %. 7. The method according to claim 1 , wherein the unstretched thermoplastic resin film is a layered film comprising a plurality of thermoplastic resin layers, and wherein the thermoplastic resin layer exposed on at least one surface comprises a thermoplastic resin in which a melt mass flow rate measured at 230° C., with a load of 3.8 kg, for 10 minutes is 10 to 15 g/10 min. 8. The method according to claim 1 , wherein the unstretched thermoplastic resin film is a layered film comprising a plurality of thermoplastic resin layers, and wherein the thermoplastic resin layer exposed on at least one surface comprises fine particles.
Manufacture of films or sheets · CPC title
Use of PC, i.e. polycarbonates {or derivatives thereof}, as moulding material · CPC title
comprising polycarbonates · CPC title
comprising vinyl {(co)polymers; comprising acrylic (co)polymers} · CPC title
Homopolymers or copolymers of methyl methacrylate · CPC title
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