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US4806299A Expired / Lapsed US ⏱️ 0.0 years remaining

Process of producing delustered nylon fiber containing segmented striations of polypropylene

Assignee: Invista North America LLC
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Filing: 1987-05-05
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Granted: 1989-02-21
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Expires: 2007-05-05
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Abstract

Abstract Small amounts of selected low molecular weight polypropylene effectively delusters drawn nylon filaments when drawn at a temperature not exceeding the softening point of the polypropylene.

Inventors

  • 👤 John T. Burns

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 12:58
CPC Classifications
D; D01; D01F; D01F6/00; D01F6/88; D01F6/90; D01F1/00; D01F1/02; D01F1/10

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 110 words
A process for producing delustered nylon filaments containing polypropylene, said polypropylene being present in generally cylindrical segmented striations having an L'/D ratio of from 1 to 10 and running generally parallel to the filament axis, comprising the steps of combining a melt of nylon with from about 0.1 to 5% by weight of a melt of polypropylene having a melting point above 120° C., a softening point below said melting point, a molecular weight of 2000-40,000, and a viscosity of 200-10,000 cP at 190° C. to form a blend, melt-spinning the blend to form filaments, quenching the filaments, and drawing the filaments at a temperature not exceeding said softening point.
Claim 2
Dependent Claim 110 words
A process for producing delustered nylon filaments containing polypropylene, said polypropylene being present in generally cylindrical segmented striations having an L'/D ratio of from 1 to 10 and running generally parallel to the filament axis, comprising the steps of combining a melt of nylon with from about 0.1 to 5% by weight of a melt of polypropylene having a melting point above 120° C., a softening point below said melting point, a molecular weight of 2000-40,000, and a viscosity of 200-10,000 cP at 190° C. to form a blend, melt-spinning the blend to form filaments, quenching the filaments, and drawing the filaments at a temperature not exceeding said softening point.
Claim 3
Dependent Claim 12 words
The process of claim 1 wherein the nylon used is polyhexamethylene adipamide.
Claim 4
Dependent Claim 18 words
The process of claim 1 wherein the nylon contains from about 0.10 to 0.35% of TiO 2 .
Claim 5
Dependent Claim 22 words
The process of claim 2 wherein the polypropylene has a molecular weight of 2000-12,000 and a viscosity of 200-2000 at 190° C.
Claim 6
Dependent Claim 36 words
The process of claim 2 wherein the polypropylene has a molecular weight of about 4500, a melting point of about 158° C., a viscosity of about 575 cP and a softening point of about 146° C.

References Cited (Backward Citations)

US2861319A Cited
US3359344A Cited
US3373224A Cited
US3471426A Cited
US3531368A Cited
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US3616184A Cited
GB1291838A Cited
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US4711812A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1992-02-21 1992-08-22 1993-02-21 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1996-02-21 1996-08-22 1997-02-21 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2000-02-21 2000-08-22 2001-02-21 $7700.00 Window Closed / Lapsed

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