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Biaxially drawn polyhexamethylene adipamide film and process for producing same

Assignee: Asahi Kasei Corp
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Filing: 1980-05-14
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Granted: 1982-10-05
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Expires: 2000-05-14
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Abstract

Abstract Disclosed is a biaxially drawn polyhexamethylene adipamide film having a relative viscosity of at least 3.2 as measured at 25° C. in aqueous 96% H 2 SO 4 , a degree of crystallinity of from 35% to 45%, a birefringence (Δn) of not more than 0.006, as determined at any point in its entire area, and an initial modulus of elasticity in tension of at least 230 kg/mm 2 as determined in ay direction across substantially its entire area. The film may be produced by a process wherein molten polyhexamethylene adipamide is extruded through a circular die gap and the tubular extrudate is brought in sliding contact with the outer periphery of an inside mandrel, thereby to be cooled, which process is characterized in that polyhexamethylene adipamide having a relative viscosity of from 3.3 to 5.0, as measured at 25° C. in aqueous 96% H 2 SO 4 , is used; the tubular extrudate formed therefrom is cooled at a cooling rate (X° C./sec.) satisfying the following formula with respect to the relative viscosity of the polymer used, -100×ηrel+1,200<X<-170×ηrel+2,150 at least in the cooling stage in which the tubular extrudate is cooled from 250° C. to 150° C., and; then, the obtained tubular film is concurrently biaxially drawn.

Inventors

  • 👤 Yukinori Matsuoka
  • 👤 Yoshihiko Muto
  • 👤 Mitsuo Kohno

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-24 16:33
CPC Classifications
B; B29; B29C; B29C48/00; B29C48/03; B29C48/09; B29C48/10; B29C48/001; B29C48/0018; B29C48/0019

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 131 words
A process for producing a biaxially drawn polyhexamethylene adipamide film wherein molten polyhexamethylene adipamide is extruded through a circular die gap and the tubular extrudate is brought in sliding contact with the outer periphery of an inside mandrel thereby to be cooled, characterized in that polyhexamethylene adipamide having a relative viscosity (ηrel) of from 3.3 to 5.0, as measured at a temperature of 25° C. in aqueous 96% sulfuric acid, is used, and the tubular extrudate formed therefrom is cooled at a cooling rate (X° C./sec.) satisfying the following formula with respect to the relative viscosity (ηrel) of the polymer used, -100×ηrel+1,200<X<-170×ηrel+2,150 at least in the cooling stage in which the tubular extrudate is cooled from 250° C. to 150° C.; and then, the obtained tubular film is concurrently biaxially drawn.
Claim 2
Dependent Claim 131 words
A process for producing a biaxially drawn polyhexamethylene adipamide film wherein molten polyhexamethylene adipamide is extruded through a circular die gap and the tubular extrudate is brought in sliding contact with the outer periphery of an inside mandrel thereby to be cooled, characterized in that polyhexamethylene adipamide having a relative viscosity (ηrel) of from 3.3 to 5.0, as measured at a temperature of 25° C. in aqueous 96% sulfuric acid, is used, and the tubular extrudate formed therefrom is cooled at a cooling rate (X° C./sec.) satisfying the following formula with respect to the relative viscosity (ηrel) of the polymer used, -100×ηrel+1,200<X<-170×ηrel+2,150 at least in the cooling stage in which the tubular extrudate is cooled from 250° C. to 150° C.; and then, the obtained tubular film is concurrently biaxially drawn.
Claim 3
Dependent Claim 20 words
The process according to claim 1 wherein the polyhexamethylene adipamide has a relative viscosity (ηrel) of from 3.5 to 4.8.
Claim 4
Dependent Claim 44 words
The process according to claim 1 wherein the biaxial drawing of the tubular film is effected concurrently, in the longitudinal (machine) direction and in the transverse direction while the parameter α, defined in the specification, is maintained at a bubble satisfying the formula: 2.5≦α<8.0
Claim 5
Dependent Claim 45 words
The process according to claim 1 wherein the biaxial drawing of the tubular film is effected at a temperature of from 70° to 180° C. and at a drawing ratio of from 2.5 to 4.0 both in the longitudinal (machine) direction and the transverse direction.
Claim 6
Dependent Claim 46 words
The process according to anyone of claims 1, 3 and 4 wherein the biaxially drawn film is further heat-treated under the conditions satisfying the formulae: 19≦ T(°C.)<240 -78.9·log t+268≦T(°C.)≦-106.8·log t+388 wherein T is a heating temperature in °C. and t is a heating period in second.
Claim 7
Dependent Claim 14 words
A biaxially drawn polyhexamethylene adipamide film obtained by the process according to claim 5.

References Cited (Backward Citations)

US3304352A Cited
US3400184A Cited
US3502766A Cited
US3794547A Cited
US3510552A Cited
US3632728A Cited
US3608019A Cited
US3788503A Cited
US3950466A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1985-10-04 1986-04-05 1986-10-05 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1989-10-04 1990-04-05 1990-10-05 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1993-10-04 1994-04-05 1994-10-05 $7700.00 Window Closed / Lapsed

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