Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
118 words
A process for producing a polypropylene film for electrical devices which comprises: biaxially stretching an unstretched isotactic polypropylene molded article, wherein the polypropylene is devoid of β-form nucleating agent and has an isotacticity of at least 90%, having, on at least one side, a surface layer containing β-form crystals of which the mean diameter is from 7 to 100 μm and the density of said crystals is at least 1000/cm 2 and being devoid of β-form crystals in the interior thereof under such conditions that the stretching temperature at the stretch initiation point is in the range of 145° to 176° C. and the stretch ratio in one direction is a factor of 3 to less than 8.
Claim 2
Dependent Claim
118 words
A process for producing a polypropylene film for electrical devices which comprises: biaxially stretching an unstretched isotactic polypropylene molded article, wherein the polypropylene is devoid of β-form nucleating agent and has an isotacticity of at least 90%, having, on at least one side, a surface layer containing β-form crystals of which the mean diameter is from 7 to 100 μm and the density of said crystals is at least 1000/cm 2 and being devoid of β-form crystals in the interior thereof under such conditions that the stretching temperature at the stretch initiation point is in the range of 145° to 176° C. and the stretch ratio in one direction is a factor of 3 to less than 8.
Claim 3
Dependent Claim
22 words
The process of claim 1, wherein the β-form crystals of the surface layer of said unstretched polypropylene molded article is β-form spherulite.
Claim 4
Dependent Claim
31 words
The process of claim 2, wherein the distribution density of the β-form crystals of said surface layer of said unstretched polypropylene molded article is more than 5,000 per cm 2 .
Claim 5
Dependent Claim
119 words
The process of claim 3, wherein said unstretched polypropylene molded article is prepared by melt-extruding a crystalline polypropylene material which does not contain a β-form crystallization nucleating agent through a ring die in the shape of a tubular melt; instantaneously or intermittently sliding the inner surface of said melt in contact with the outer periphery of at least one disc-like member which possess a slight roundness at the outer periphery, while maintaining the inner surface of said melt at a temperature in the range of 130° to 200° C.; simultaneously cooling the outer surface of said melt with a cooling medium maintained at a temperature in excess of 40° C.; and then taking up the resulting unstretched molded article.
Claim 6
Dependent Claim
33 words
The process of claim 1, wherein the β-form crystals of the surface layer of the unstretched polypropylene molded article are of a pillar-like β-form crystal, which are aligned in the direction of extrusion.
Claim 7
Dependent Claim
30 words
The biaxially stretched isotactic polypropylene film prepared by the process of Claim 1, wherein said polypropylene is devoid of β-form nucleating agent and has an isotacticity of at least 90%,
Claim 8
Dependent Claim
95 words
The process of claim 5, wherein said unstretched polypropylene molded article is prepared by melt-extruding a crystalline polypropylene material which does not contain a β-form crystallization nucleating agent through a ring die in the shape of a tubular melt; sliding the inner surface of said melt in contact with a cylindrical member maintained at a temperature in the range of 30° to 110° C.; simultaneously cooling the outer surface of said melt with a cooling medium at a temperature below the temperature of said cylindrical member; and then taking up the resulting unstretched molded article.
Claim 9
Dependent Claim
131 words
The process of claim 5, wherein said unstretched polypropylene molded article is prepared by melt-extruding a crystalline polypropylene material which does not contain a β-form crystalline nucleating agent through a ring die, under such conditions that the resin temperature at the time of extrusion from the die orifice is a temperature up to 230° C. and the average extrusion linear velocity from the die orifice is at least 1.5 cm/sec. in the shape of a tubular melt, contacting the outer surface of said melt with a first cooling medium having a temperature of 45° C. to 130° C.; simultaneously contacting the inner surface of said melt with a second cooling medium having a temperature lower than that of said first cooling medium and then taking up the resulting unstretched molded article.