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US4239822A Expired / Lapsed US ⏱️ 0.0 years remaining

Propylene/polystyrene composition and method for coating

Assignee: Rexam Beverage Can Co
•
Filing: 1979-06-22
•
Granted: 1980-12-16
•
Expires: 1999-06-22
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Abstract

Abstract Melt extrudable polypropylene-polystyrene compositions are provided which are particularly suitable for use in extrusion coating. Substrates coated with such compositions as well as methods of producing such coated substrates are also provided.

Inventors

  • 👤 Theodore L. McGee

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 15:50
CPC Classifications
D; D21; D21H; D21H19/00; D21H19/10; D21H19/14; D21H19/20; D21H19/22; B; B05; B05D; B05D1/00; B05D1/26; B05D1/265; B05D7/00; B05D7/02; C; C09; C09D; C09D123/00; C09D123/02; C09D123/10; C09D123/12; C09D125/00; C09D125/02; C09D125/04; C09D125/06; C08; C08L; C08L23/00; C08L23/02; C08L23/10; C08L23/12; Y; Y10; Y10T; Y10T428/00; Y10T428/31504; Y10T428/31855; Y10T428/3188; Y10T428/31895

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 116 words
A process of coating a substrate with an extruded film of a polymer blend comprising: providing a blend of polystyrene and a polypropylene having a melt flow rate, as determined by ASTM-1238-G, within the range of about 30 to about 40 grams per ten minutes, the ratio of polypropylene to polystyrene in the blend being within the range of about 5:1 to 2:1; extruding said polymer blend without substantial degradation at a melt temperature of about 475° F. to about 575° F. to contact said substrate; passing said coated substrate to contact a chill roll maintained at a temperature of about 120°-200° F. to form an adhered layer of said extruded polymer blend on said substrate.
Claim 2
Dependent Claim 116 words
A process of coating a substrate with an extruded film of a polymer blend comprising: providing a blend of polystyrene and a polypropylene having a melt flow rate, as determined by ASTM-1238-G, within the range of about 30 to about 40 grams per ten minutes, the ratio of polypropylene to polystyrene in the blend being within the range of about 5:1 to 2:1; extruding said polymer blend without substantial degradation at a melt temperature of about 475° F. to about 575° F. to contact said substrate; passing said coated substrate to contact a chill roll maintained at a temperature of about 120°-200° F. to form an adhered layer of said extruded polymer blend on said substrate.
Claim 3
Dependent Claim 31 words
A process as claimed in claim 1 wherein said extrudate exits a 30 mil die and is drawn down to a thickness within the range of about 0.3 to 1 mil.
Claim 4
Dependent Claim 39 words
A process as claimed in claim 2 wherein said polymer blend comprises from about 50 to 70% by weight of polypropylene, from about 10 to 30% by weight of polystyrene and up to 10% by weight of a pigment.
Claim 5
Dependent Claim 45 words
A process as claimed in claim 2 wherein said polymer blend comprises from about 50% to 70% by weight polypropylene, from about 10 to 30% by weight polystyrene and from about 5 to 30% by weight of a concentrate of pigment in a polyethylene carrier.
Claim 6
Dependent Claim 10 words
The process of claim 1 wherein said substrate is paperboard.

References Cited (Backward Citations)

US3018263A Cited
US3271354A Cited
US3092891A Cited
US3173163A Cited
US3666834A Cited
US3652725A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-12-16 1984-06-16 1984-12-16 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-12-16 1988-06-16 1988-12-16 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-12-16 1992-06-16 1992-12-16 $7700.00 Window Closed / Lapsed

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