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US4053674A Expired / Lapsed US ⏱️ 0.0 years remaining

Glow-resistant batt and process for producing such

Assignee: Fiberlok Inc
•
Filing: 1975-09-12
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Granted: 1977-10-11
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Expires: 1995-09-12
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Abstract

Abstract A glow-resistant batt of fibers; a copolymer of vinyl chloride and vinylidene chloride; and boric acid; and processes for producing such.

Inventors

  • 👤 George Sumner Buck, Jr.
  • 👤 Robert George Weyker
  • 👤 Arthur Gerard Ward

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-07 20:39
CPC Classifications
D; D04; D04H; D04H1/00; D04H1/40; D04H1/58; D04H1/60; Y; Y10; Y10S; Y10S428/00; Y10S428/92; Y10T; Y10T428/00; Y10T428/25; Y10T428/254; Y10T428/26; Y10T428/269; Y10T428/29; Y10T428/2904; Y10T428/2905; Y10T428/2913; Y10T428/2927; Y10T442/00; Y10T442/20; Y10T442/2631; Y10T442/2664; Y10T442/60; Y10T442/699

Claims Analysis

Total Claims: 13
Claim 1
Independent Claim 157 words
A process for producing a batt comprising the steps of: I. forming a thin web of fibers; Ii. contacting the web with an adhesive amount of particles of a copolymer of vinyl chloride and vinylidene chloride; Iii. contacting the web with a glow-resistance imparting amount of boric acid; Iv. forming the web into a batt by laying the web transversely back and forth on a moving belt such that the batt comprises a plurality of webs; and V. heating the batt to a temperature above the sticking point of the copolymer but below the degredation point of the fibers wherein the weight ratio of vinyl chloride to vinylidene chloride is 1:99 to 40:60 and wherein the weight ratio of the copolymer to the fibers is 1:99 to 30:70 and wherein the copolymer particles have a size range of from 1 to 200 microns and wherein the weight ratio of copolymer to boric acid is 5:10 to 200:10.
Claim 2
Dependent Claim 157 words
A process for producing a batt comprising the steps of: I. forming a thin web of fibers; Ii. contacting the web with an adhesive amount of particles of a copolymer of vinyl chloride and vinylidene chloride; Iii. contacting the web with a glow-resistance imparting amount of boric acid; Iv. forming the web into a batt by laying the web transversely back and forth on a moving belt such that the batt comprises a plurality of webs; and V. heating the batt to a temperature above the sticking point of the copolymer but below the degredation point of the fibers wherein the weight ratio of vinyl chloride to vinylidene chloride is 1:99 to 40:60 and wherein the weight ratio of the copolymer to the fibers is 1:99 to 30:70 and wherein the copolymer particles have a size range of from 1 to 200 microns and wherein the weight ratio of copolymer to boric acid is 5:10 to 200:10.
Claim 3
Dependent Claim 12 words
The process of claim 1 wherein the thin web is horizontally disposed.
Claim 4
Dependent Claim 17 words
The process of claim 1 wherein the copolymer has a sticking point of 300° to 370° F.
Claim 5
Dependent Claim 17 words
The process of claim 1 wherein the temperature in step V is between 300° and 400° F.
Claim 6
Dependent Claim 19 words
The process of claim 1 wherein the heating is conducted for a period of from 1 to 20 minutes.
Claim 7
Dependent Claim 10 words
The process of claim 1 wherein the fibers are cotton.
Claim 8
Dependent Claim 15 words
The process of claim 1 wherein the fibers are a blend of cotton and polyester.
Claim 9
Dependent Claim 22 words
The process of claim 1 wherein the copolymer and the boric acid are contacted with the web in admixture with each other.
Claim 10
Dependent Claim 307 words
A completely dry process for producing a batt of high compressive strength comprising in sequence the steps of: I. forming a horizontally disposed, thin, planar web of fibers; Ii. contacting the web with particles of a copolymer of vinyl chloride and vinylidene chloride in admixture with boric acid while the web is in contact with and supported by a moving belt thereby inhibiting the passage of particles through the web; A. wherein the weight ratio of vinyl chloride to vinylidene chloride is 5:95 to 25:75, B. wherein the weight ratio of the copolymer to the fibers is 10:90 to 20:80, C. wherein the copolymer particles have a size range of 5 microns to 50 microns, D. wherein the copolymer has a sticking point of 300° to 370° F., E. wherein the boric acid comprises from 2 to 6 weight percent of the batt, F. wherein the weight ratio of copolymer to boric acid is 2:1 to 10:1, G. wherein the particles are fed from a container onto a first rotating member which is then contacted with a counter-rotating brush having bristles which remove the particles from the first rotating member permitting the particles to fall on the web under the influence of gravity, Iii. passing the web and adhering particles through the nip of two rotating rolls to impress the particles into the web; Iv. forming the web into a batt by laying the web transversely back and forth on a moving belt such that the batt comprises a plurality of webs; V. heating the batt to a temperature of 325° to 375° F. for a period of 2 to 10 minutes while the batt is being passed through an oven between two parallel foraminous belts while hot air is forced through the belts and through the batt; thereby providing a glow-resistant batt of high compressive strength.
Claim 11
Dependent Claim 307 words
A completely dry process for producing a batt of high compressive strength comprising in sequence the steps of: I. forming a horizontally disposed, thin, planar web of fibers; Ii. contacting the web with particles of a copolymer of vinyl chloride and vinylidene chloride in admixture with boric acid while the web is in contact with and supported by a moving belt thereby inhibiting the passage of particles through the web; A. wherein the weight ratio of vinyl chloride to vinylidene chloride is 5:95 to 25:75, B. wherein the weight ratio of the copolymer to the fibers is 10:90 to 20:80, C. wherein the copolymer particles have a size range of 5 microns to 50 microns, D. wherein the copolymer has a sticking point of 300° to 370° F., E. wherein the boric acid comprises from 2 to 6 weight percent of the batt, F. wherein the weight ratio of copolymer to boric acid is 2:1 to 10:1, G. wherein the particles are fed from a container onto a first rotating member which is then contacted with a counter-rotating brush having bristles which remove the particles from the first rotating member permitting the particles to fall on the web under the influence of gravity, Iii. passing the web and adhering particles through the nip of two rotating rolls to impress the particles into the web; Iv. forming the web into a batt by laying the web transversely back and forth on a moving belt such that the batt comprises a plurality of webs; V. heating the batt to a temperature of 325° to 375° F. for a period of 2 to 10 minutes while the batt is being passed through an oven between two parallel foraminous belts while hot air is forced through the belts and through the batt; thereby providing a glow-resistant batt of high compressive strength.
Claim 12
Dependent Claim 88 words
A glow-resistant fibrous batt comprising: A. fibers bonded at their intersections by melted particles of a copolymer of vinyl chloride and vinylidene chloride wherein the weight ratio of vinyl chloride to vinylidene chloride is 1:99 to 40:60 and wherein the weight ratio of the copolymer to the fibers is 1:99 to 30:70 and wherein the copolymer particles have a size range of from 1 to 200 microns and; B. boric acid carried by the copolymer wherein the weight ratio of copolymer to boric acid is 5:10 to 200:10.
Claim 13
Dependent Claim 88 words
A glow-resistant fibrous batt comprising: A. fibers bonded at their intersections by melted particles of a copolymer of vinyl chloride and vinylidene chloride wherein the weight ratio of vinyl chloride to vinylidene chloride is 1:99 to 40:60 and wherein the weight ratio of the copolymer to the fibers is 1:99 to 30:70 and wherein the copolymer particles have a size range of from 1 to 200 microns and; B. boric acid carried by the copolymer wherein the weight ratio of copolymer to boric acid is 5:10 to 200:10.

References Cited (Backward Citations)

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US2568144A Cited
US2808098A Cited
US2972554A Cited
US3033726A Cited
US3117055A Cited
US3369948A Cited
US3498875A Cited
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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) 1980-10-10 1981-04-11 1981-10-11 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-10-10 1985-04-11 1985-10-11 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-10-10 1989-04-11 1989-10-11 $7700.00 Window Closed / Lapsed

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