US5112424A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Low temperature multi-layer extrusion coating process
Assignee: Eastman Chemical Co
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Filing: 1989-09-01
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Granted: 1992-05-12
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Expires: 2009-09-01
Abstract
Abstract Process for applying multi-layer extrusion coatings to substrate at low temperature is described, employing as one extrusion coating layer a defined polyethylene-containing component, and, as the second extrusion coating layer at least one second extrudable polymeric composition. Also provided are novel extrusion coated articles comprising substrate having coated thereon defined polyethylene-containing component and at least one other extrudable polymeric composition. These articles display good adhesion of extrusion coating material to the substrate without the degradation of the extrudable coatings caused by exposure to excessive levels of heat as is required for successful extrusion coating employing prior art materials.
Inventors
- 👤 John W. Cook
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 17:21
CPC Classifications
B; B05; B05D; B05D7/00; B05D7/50; B05D7/52; B05D7/54; B05D7/548; B05D7/5483; B05D7/5485; B05D1/00; B05D1/26; B05D2507/00; B05D2507/01
Claims Analysis
Total Claims: 20
Claim 1
Independent Claim
322 words
A process for the low-temperature multi-layer extrusion coating of a substrate with a first, polyethylene-coating layer which is subjected to a temperature no greater than about 480° F., and at least one additional layer comprising at least one second extrudable composition, said process comprising: applying to at least one surface of said substrate a polyethylene-containing composition to form said first, polyethylene-containing layer, comprising: (a) a polyethylene component having a melt index in the range of about 10 up to 100 dg per minute at 190° C. and having a sufficiently broad molecular weight distribution so that the resulting composition is capable of being extrusion coated at a temperature less than about 480° F. to a thickness as thin as 0.0003 inches (0.0075 mm) at a speed of at least 1000 feet per minute (300 meters per minute), and (b) in the range of about 5 up to 15 wt %, based on the weight of the total composition, of a hydrocarbon tackifying resin having a Ring and Ball Softening Point in the range of about 125° up to 140° C., and at least one second extrudable composition selected from: polyethylenes having a melt index different than the melt index of said first polyethylene component, polyethylenes having a density different than the density of said first polyethylene component, polyethylenes modified with polymer additives, polypropylene homopolymers, comonomers, copolymers, and terpolymers, optionally modified with polymer additives, polyethylene comonomers, copolymers and terpolymers, including extrudable ionomers, optionally modified with polymer additives, extrudable polymers of higher olefins having in the range of 4 up to 8 carbon atoms, optionally modified with polymer additives, extrudable polyvinylidene chloride, optionally modified with polymer additives, extrudable polyamides, optionally modified with polymer additives, or extrudable polyesters, optionally modified with polymer additives; wherein said process is carried out by multi-layer extrusion coating of said substrate; and wherein the temperature of said polyethylene-containing composition is no greater than about 480° F. during the extrusion process.
Claim 2
Dependent Claim
322 words
A process for the low-temperature multi-layer extrusion coating of a substrate with a first, polyethylene-coating layer which is subjected to a temperature no greater than about 480° F., and at least one additional layer comprising at least one second extrudable composition, said process comprising: applying to at least one surface of said substrate a polyethylene-containing composition to form said first, polyethylene-containing layer, comprising: (a) a polyethylene component having a melt index in the range of about 10 up to 100 dg per minute at 190° C. and having a sufficiently broad molecular weight distribution so that the resulting composition is capable of being extrusion coated at a temperature less than about 480° F. to a thickness as thin as 0.0003 inches (0.0075 mm) at a speed of at least 1000 feet per minute (300 meters per minute), and (b) in the range of about 5 up to 15 wt %, based on the weight of the total composition, of a hydrocarbon tackifying resin having a Ring and Ball Softening Point in the range of about 125° up to 140° C., and at least one second extrudable composition selected from: polyethylenes having a melt index different than the melt index of said first polyethylene component, polyethylenes having a density different than the density of said first polyethylene component, polyethylenes modified with polymer additives, polypropylene homopolymers, comonomers, copolymers, and terpolymers, optionally modified with polymer additives, polyethylene comonomers, copolymers and terpolymers, including extrudable ionomers, optionally modified with polymer additives, extrudable polymers of higher olefins having in the range of 4 up to 8 carbon atoms, optionally modified with polymer additives, extrudable polyvinylidene chloride, optionally modified with polymer additives, extrudable polyamides, optionally modified with polymer additives, or extrudable polyesters, optionally modified with polymer additives; wherein said process is carried out by multi-layer extrusion coating of said substrate; and wherein the temperature of said polyethylene-containing composition is no greater than about 480° F. during the extrusion process.
Claim 3
Dependent Claim
21 words
A process in accordance with claim 1 wherein said first, polyethylene-containing layer has a thickness no greater than about 0.0075 mm.
Claim 4
Dependent Claim
83 words
A process in accordance with claim 1 wherein said at least one second extrudable composition is selected from: polyethylenes having a melt index different than the melt index of said first polyethylene component, polyethylenes having a density different than the density of said first polyethylene component, polyethylenes modified with polymer additives, polypropylene homopolymers, comonomers, copolymers, and terpolymers, optionally modified with polymer additives, polyethylene comonomers, copolymers and terpolymers, including extrudable ionomers, optionally modified with polymer additives, or extrudable polyamides, optionally modified with polymer additives.
Claim 5
Dependent Claim
26 words
A process in accordance with claim 3 wherein said extrusion coating process is capable of substantially uniformly coating at least 300 m per minute of substrate.
Claim 6
Dependent Claim
51 words
A process in accordance with claim 1 wherein said at least one second extrudable composition is a heat sealable composition selected from: polyethylene having a melt index lower than the melt index of said first polyethylene component, or polyethylene comonomers, copolymers and terpolymers, including extrudable ionomers, optionally modified with polymer additives.
Claim 7
Dependent Claim
49 words
A process in accordance with claim 1 wherein said at least one second extrudable composition provides a barrier layer, and is selected from: polyethylene comonomers, copolymers and terpolymers, optionally modified with polymer additives, extrudable polyvinylidene chloride, optionally modified with polymer additives, or extrudable polyamides, optionally modified with polymer additives.
Claim 8
Dependent Claim
66 words
A process in accordance with claim 1 wherein said at least one second extrudable composition is selected from: polyethylene comonomers, copolymers and terpolymers with at least one co-monomer selected from: vinyl acetate, vinyl alcohol, carbon monoxide, maleic anhydride, ethyl methyl acrylate, ethyl ethyl acrylate, ethyl methyl pentene, or ethyl acrylic acid, wherein each of said polyethylene copolymers and terpolymers can optionally be modified with polymer additives.
Claim 9
Dependent Claim
21 words
A process in accordance with claim 1 wherein said substrate is selected from: papers, paperboards, fibers, polymeric materials, or metal foils.
Claim 10
Dependent Claim
33 words
A process in accordance with claim 8 wherein said polymeric materials are selected from: polyolefins or functionally modified polyolefins, polyesters or functionally modified polyesters, ethylene-vinyl alcohol copolymers, or polyamides or functionally modified polyamides.
Claim 11
Dependent Claim
27 words
A process in accordance with claim 1 wherein said polyethylene component has a melt index in the range of about 20 up to 80 dg per minute.
Claim 12
Dependent Claim
19 words
A process in accordance with claim 1 wherein said polyethylene component has a density of at least 0.915 g/cc.
Claim 13
Dependent Claim
34 words
A process in accordance with claim 1 wherein said hydrocarbon tackifying resin is selected from polymerized β-pinenes, hydrogenated polymers of C 5 hydrocarbons, α-methyl styrene-vinyl toluene copolymers or pentaerythritol esters of tall oil rosin.
Claim 14
Dependent Claim
24 words
A process in accordance with claim 1 containing in the range of about 7 up to 10 wt % of said hydrocarbon tackifying resin.
Claim 15
Dependent Claim
15 words
A process in accordance with claim 13 wherein said tackifying resin is a polymerized β-pinene.
Claim 16
Dependent Claim
19 words
A process in accordance with claim 1 wherein said first polyethylene-containing layer is the layer that contacts the substrate.
Claim 17
Dependent Claim
17 words
A process in accordance with claim 1 wherein said first polyethylene-containing layer is an exterior barrier layer.
Claim 18
Dependent Claim
19 words
A process in accordance with claim 1 comprising said first polyethylene-containing layer and at least two additional extrudable compositions.
Claim 19
Dependent Claim
21 words
A process in accordance with claim 17 wherein said first polyethylene-containing layer is an adhesive tie-layer between two additional extrudable compositions.
Claim 20
Dependent Claim
23 words
A process in accordance with claim 1 wherein said polyethylene-containing composition has a differential scanning calorimetry curve substantially as shown in FIG. 1.
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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) | 1995-05-12 | 1995-11-11 | 1996-05-12 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1999-05-12 | 1999-11-11 | 2000-05-12 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2003-05-12 | 2003-11-11 | 2004-05-12 | $7700.00 | Window Closed / Lapsed |