US4455273A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Producing modified high performance polyolefin fiber
Assignee: Honeywell International Inc
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Filing: 1982-09-30
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Granted: 1984-06-19
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Expires: 2002-09-30
Abstract
Abstract Fibers prepared by spinning, drawing and drying dilute solutions of ultrahigh molecular weight polyethylene or polypropylene are modified by including in the dilute solution a polymeric additive. The polyethylene fibers so prepared have melting points above 140 DEG C. and exhibit improved adherence to matrices, resistance to fibrillation and other advantageous properties. Additives include lower molecular weight polyolefins, oxidized polyolefins, olefin copolymers, polyolefin graft copolymers and polyoxymethylenes.
Inventors
- 👤 Gary A. Harpell
- 👤 Sheldon Kavesh
- 👤 Igor Palley
- 👤 Dusan C. Prevorsek
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-23 20:18
CPC Classifications
C; C08; C08J; C08J5/00; C08J5/04; C08J5/046; B; B29; B29C; B29C48/00; B29C48/022; D; D01; D01F; D01F6/00; D01F6/02; D01F6/04; D01F6/44; D01F6/46; B29C48/03; B29C48/05; B29K; B29K2023/00; B29K2023/04; B29K2023/06; B29K2105/00; B29K2105/0058; B29K2105/0073; B29K2223/00; B29K2223/04; B29K2223/06; C08J2363/00
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
212 words
A process of forming a high tenacity, high modulus polyethylene or polypropylene fiber, in which (a) a dilute solution of ultrahigh molecular weight polyethylene or polypropylene in a first solvent is spun and cooled to form a first gel fiber, (b) the gel fiber is extracted (if said first solvent is non-volatile) with a volatile solvent to form a second gel fiber, (c) the first gel fiber (if said first solvent is volatile) or the second gel fiber is dried to form a xerogel fiber and (d) at least one of the first gel fiber, the second gel fiber and the xerogel fiber is stretched; characterized by the dilute solution comprising the ultrahigh molecular weight polyethylene or polypropylene, the solvent and a polymeric additive selected from the group consisting of copolymers containing monoolefins as primary monomers, polyolefins of molecular weight not greater than 250,000, oxidized polyolefins, graft polyolefin copolymers, and polyoxymethylenes, with the weight of polymeric additive being at least 2% of the weight of ultrahigh molecular weight polyethylene or polypropylene, but not being sufficiently high to lower the main melting temperature of the product fiber (by DSC in argon at 10° C./min) to below 140° C. in the case of polyethylene or to below 162° C. in the case of polypropylene.
Claim 2
Dependent Claim
212 words
A process of forming a high tenacity, high modulus polyethylene or polypropylene fiber, in which (a) a dilute solution of ultrahigh molecular weight polyethylene or polypropylene in a first solvent is spun and cooled to form a first gel fiber, (b) the gel fiber is extracted (if said first solvent is non-volatile) with a volatile solvent to form a second gel fiber, (c) the first gel fiber (if said first solvent is volatile) or the second gel fiber is dried to form a xerogel fiber and (d) at least one of the first gel fiber, the second gel fiber and the xerogel fiber is stretched; characterized by the dilute solution comprising the ultrahigh molecular weight polyethylene or polypropylene, the solvent and a polymeric additive selected from the group consisting of copolymers containing monoolefins as primary monomers, polyolefins of molecular weight not greater than 250,000, oxidized polyolefins, graft polyolefin copolymers, and polyoxymethylenes, with the weight of polymeric additive being at least 2% of the weight of ultrahigh molecular weight polyethylene or polypropylene, but not being sufficiently high to lower the main melting temperature of the product fiber (by DSC in argon at 10° C./min) to below 140° C. in the case of polyethylene or to below 162° C. in the case of polypropylene.
Claim 3
Dependent Claim
18 words
The process of claim 1 wherein said dilute solution contains ultrahigh molecular weight polyethylene and an ethylene copolymer.
Claim 4
Dependent Claim
29 words
The process of claim 2 wherein said ethylene copolymer contains at least one comonomer selected from the group consisting of acrylic acid, methacrylic acid, vinyl acetate and vinyl alcohol.
Claim 5
Dependent Claim
20 words
The process of claim 3 wherein said ethylene copolymer is an ethylene-acrylic acid copolymer with 1-15 mole percent acrylic acid.
Claim 6
Dependent Claim
13 words
The process of claim 2 wherein the ethylene copolymer is an ethylene-propylene copolymer.
Claim 7
Dependent Claim
13 words
The process of claim 2 wherein the ethylene copolymer is an ethylene-propylene-diene terpolymer.
Claim 8
Dependent Claim
27 words
The process of claim 1 wherein said dilute solution contains ultrahigh molecular weight polyethylene and, as polymeric additive, a polyolefin of molecular weight not greater than 250,000.
Claim 9
Dependent Claim
13 words
The process of claim 7 wherein said polymeric additive is low density polyethylene.
Claim 10
Dependent Claim
16 words
The process of claim 7 wherein the polyolefin is of molecular weight not greater than 100,000.
References Cited (Backward Citations)
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1987-06-19 | 1987-12-19 | 1988-06-19 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-06-19 | 1991-12-19 | 1992-06-19 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-06-19 | 1995-12-19 | 1996-06-19 | $7700.00 | Window Closed / Lapsed |