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US3962388A Expired / Lapsed US ⏱️ 0.0 years remaining

Method of producing a foam fibrillated web

Assignee: Sun Research and Development Co
•
Filing: 1973-01-02
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Granted: 1976-06-08
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Expires: 1993-01-02
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Abstract

Abstract Non-woven fabrics are produced from oriented foam fibrillated webs containing 75 to 98 wt. % polypropylene and 2 to 25 wt. % of an ethylene-vinyl acetate copolymer containing from 2 to 40 wt. % vinyl acetate and 60 to 98 wt. % ethylene. The webs are assembled in a plurality of layers and then bonded by heat and pressure either with or without the presence of an adhesive. In a preferred aspect films especially of polyethylene or ethylene-vinyl acetate copolymers are used as the bonding agent.

Inventors

  • 👤 Gary L. Driscoll

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-25 21:14
CPC Classifications
D; D04; D04H; D04H13/00; Y; Y10; Y10S; Y10S264/00; Y10S264/08; Y10S264/47; Y10S428/00; Y10S428/91; Y10T; Y10T428/00; Y10T428/24; Y10T428/24058; Y10T428/24074; Y10T428/24091; Y10T428/24273; Y10T428/24298; Y10T428/24314

Claims Analysis

Total Claims: 5
Claim 1
Independent Claim 225 words
A process of producing a foam fibrillated fibrous web comprising heating a blend of from 75 to 98 weight percent as based on said blend of isotactic polypropylene having a melt index below 30 and from 2 to 25 weight percent as based on said blend of ethylene-vinyl acetate copolymer containing from 60 to 98 weight percent ethylene and from 2 to 40 weight percent vinyl acetate and having a melt index from 1 to 400 in an extruder to from 175° to 260°C whereby a molten blend is formed, extruding said molten blend and from 0.1 to 20 percent by weight as based on said blend of a material which is gaseous under the extrusion conditions used mixed with said molten blend from a die into a zone of reduced pressure to produce an extrudate, quenching said extrudate to a temperature below about 150°C while withdrawing said extrudate from said die by a first linear take-up means at a linear rate of from 2 to 25 times the linear rate at which said blend reaches the lips of said die whereby the foam cells forming are ruptured and a foam fibrillated web is formed, and stretching said foam fibrillated web from 1.5 to 10 times in the machine direction at a temperature of from about 90°C to about 150°C to increase the strength thereof.
Claim 2
Dependent Claim 225 words
A process of producing a foam fibrillated fibrous web comprising heating a blend of from 75 to 98 weight percent as based on said blend of isotactic polypropylene having a melt index below 30 and from 2 to 25 weight percent as based on said blend of ethylene-vinyl acetate copolymer containing from 60 to 98 weight percent ethylene and from 2 to 40 weight percent vinyl acetate and having a melt index from 1 to 400 in an extruder to from 175° to 260°C whereby a molten blend is formed, extruding said molten blend and from 0.1 to 20 percent by weight as based on said blend of a material which is gaseous under the extrusion conditions used mixed with said molten blend from a die into a zone of reduced pressure to produce an extrudate, quenching said extrudate to a temperature below about 150°C while withdrawing said extrudate from said die by a first linear take-up means at a linear rate of from 2 to 25 times the linear rate at which said blend reaches the lips of said die whereby the foam cells forming are ruptured and a foam fibrillated web is formed, and stretching said foam fibrillated web from 1.5 to 10 times in the machine direction at a temperature of from about 90°C to about 150°C to increase the strength thereof.
Claim 3
Dependent Claim 19 words
The process of claim 1 wherein from 0.1 to 5.0 percent by weight of said gaseous material is used.
Claim 4
Dependent Claim 21 words
The process of claim 2 wherein the die opening is from about 15 to about 25 mils in the thickness direction.
Claim 5
Dependent Claim 25 words
The process of claim 3 wherein the blend contains about 10 weight percent ethylene-vinyl acetate copolymer and the fibrillated web is stretched about 3.35 times.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-06-08 1979-12-08 1980-06-08 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-06-08 1983-12-08 1984-06-08 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-06-08 1987-12-08 1988-06-08 $7700.00 Window Closed / Lapsed

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