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US4420448A Expired / Lapsed US ⏱️ 0.0 years remaining

Polymer foam process

Assignee: Mobil Oil AS
•
Filing: 1982-08-26
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Granted: 1983-12-13
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Expires: 2002-08-26
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Abstract

Abstract A method for treating foamed polymer comprising exposing said polymer to an atmosphere of at least substantially carbon dioxide at a temperature sufficient to cause transpiration, absorption and/or dissolution of carbon dioxide into said polymer and decrease the density thereof on subsequent heating.

Inventors

  • 👤 Charles M. Krutchen

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 16:34
CPC Classifications
C; C08; C08J; C08J9/00; C08J9/36; B; B29; B29C; B29C44/00; B29C44/34; B29C44/56; B29C44/5609; Y; Y10; Y10S; Y10S264/00; Y10S264/15

Claims Analysis

Total Claims: 23
Claim 1
Independent Claim 38 words
A method for treating foamed styrene polymer sheet comprising exposing said polymer sheet to an atmosphere of at least substantially carbon dioxide at a temperature sufficient to cause transpiration, absorption or dissolution of carbon dioxide into said polymer.
Claim 2
Independent Claim 38 words
A method for treating foamed styrene polymer sheet comprising exposing said polymer sheet to an atmosphere of at least substantially carbon dioxide at a temperature sufficient to cause transpiration, absorption or dissolution of carbon dioxide into said polymer.
Claim 3
Independent Claim 79 words
A method for decreasing the density of foamed polystyrene sheet comprising: extruding a combination of molten polystyrene and foaming agent from a region of higher pressure to a region of lower pressure to cause foaming of the polystyrene; transporting the foamed polystyrene through a confined region having an atmosphere of at least substantially carbon dioxide to thereby decrease the density of said foamed polystyrene on subsequent heating above the Tg of said resin as compared with unaged foamed resin.
Claim 4
Independent Claim 79 words
A method for decreasing the density of foamed polystyrene sheet comprising: extruding a combination of molten polystyrene and foaming agent from a region of higher pressure to a region of lower pressure to cause foaming of the polystyrene; transporting the foamed polystyrene through a confined region having an atmosphere of at least substantially carbon dioxide to thereby decrease the density of said foamed polystyrene on subsequent heating above the Tg of said resin as compared with unaged foamed resin.
Claim 5
Dependent Claim 17 words
The process of claim 2 wherein said atmosphere is at a temperature about 35° to 135° C.
Claim 6
Dependent Claim 107 words
A process for preparing rapidly aged thermoplastic resin foam sheet comprising (a) melting a thermoplastic resin; (b) introducing thereto under pressure, a foaming agent in liquid form, said agent being a member selected from the group consisting of a low molecular weight alphatic hydrocarbon, a low molecular weight halocarbon and mixtures thereof; (c) extruding the combination in sheet form into a lower pressure atmosphere of air to cause foaming of said resin; and transporting said foamed resin through a confined region having an atmosphere of at least substantially carbon dioxide to age said foamed resin at a rate faster than in the absence of the carbon dioxide.
Claim 7
Dependent Claim 107 words
A process for preparing rapidly aged thermoplastic resin foam sheet comprising (a) melting a thermoplastic resin; (b) introducing thereto under pressure, a foaming agent in liquid form, said agent being a member selected from the group consisting of a low molecular weight alphatic hydrocarbon, a low molecular weight halocarbon and mixtures thereof; (c) extruding the combination in sheet form into a lower pressure atmosphere of air to cause foaming of said resin; and transporting said foamed resin through a confined region having an atmosphere of at least substantially carbon dioxide to age said foamed resin at a rate faster than in the absence of the carbon dioxide.
Claim 8
Dependent Claim 12 words
The process of claim 4 wherein said resin is a styrene polymer.
Claim 9
Dependent Claim 11 words
The process of claim 5 wherein said polymer is a polystyrene.
Claim 10
Dependent Claim 10 words
The process of claim 5 wherein said polymer is poly-p-methylstyrene.
Claim 11
Dependent Claim 26 words
The process of claim 4 wherein a nucleating agent, in an amount effective for nucleating foam cells, is added to said resin prior to extrusion thereof.
Claim 12
Dependent Claim 18 words
The process of claim 8 wherein said nucleating agent is a mixture of citric acid and sodium bicarbonate.
Claim 13
Dependent Claim 19 words
The process of claim 4 wherein the aged, foamed polymer is thereafter thermoformed into articles without any additional aging.
Claim 14
Dependent Claim 160 words
A continuous process for preparing a thermoplastic resin foam sheet comprising: (a) feeding a thermoplastic resin to a screw-type extruder and heating the resin to a first temperature above the melting temperature of the resin; (b) introducing thereto, under pressure, a foaming agent in liquid form, while mixing the resin at said first temperature, said foaming agent being a member selected from the group consisting of a low molecular weight aliphatic hydrocarbon, a low molecular weight halocarbon and a mixture thereof; (c) cooling the mixture of molten resin and blowing agent to a second temperature below the first temperature and above the melting temperature; (d) extruding a sheet of said resin into a lower pressure atmosphere of air to cause foaming of said resin; and (e) transporting said foamed resin sheet through a confined region of substantially carbon dioxide to cause aging of said foamed resin at least at a rate faster than in the absence of said carbon dioxide.
Claim 15
Dependent Claim 160 words
A continuous process for preparing a thermoplastic resin foam sheet comprising: (a) feeding a thermoplastic resin to a screw-type extruder and heating the resin to a first temperature above the melting temperature of the resin; (b) introducing thereto, under pressure, a foaming agent in liquid form, while mixing the resin at said first temperature, said foaming agent being a member selected from the group consisting of a low molecular weight aliphatic hydrocarbon, a low molecular weight halocarbon and a mixture thereof; (c) cooling the mixture of molten resin and blowing agent to a second temperature below the first temperature and above the melting temperature; (d) extruding a sheet of said resin into a lower pressure atmosphere of air to cause foaming of said resin; and (e) transporting said foamed resin sheet through a confined region of substantially carbon dioxide to cause aging of said foamed resin at least at a rate faster than in the absence of said carbon dioxide.
Claim 16
Dependent Claim 20 words
The process of claim 11 wherein said aging on subsequent heating effects a density decrease of at least about 20%.
Claim 17
Dependent Claim 12 words
The process of claim 12 wherein said resin is a styrene polymer.
Claim 18
Dependent Claim 23 words
The process of claim 13 wherein said foaming agent is a C 1 to C 10 hydrocarbon or a fluorocarbon or mixtures thereof.
Claim 19
Dependent Claim 11 words
The process of claim 14 wherein said blowing agent is pentane.
Claim 20
Dependent Claim 10 words
The process of claim 15 wherein said resin is polystyrene.
Claim 21
Dependent Claim 10 words
The process of claim 15 wherein said resin is poly-p-methylstyrene.
Claim 22
Dependent Claim 26 words
The process of claim 16 wherein a nucleating agent, in an amount effective for nucleating foam cells, is added to said resin prior to extrusion thereof.
Claim 23
Dependent Claim 18 words
The process of claim 18 wherein said nucleating agent is a mixture of citric acid and sodium bicarbonate.

References Cited (Backward Citations)

US2774991A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1986-12-12 1987-06-13 1987-12-13 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1990-12-12 1991-06-13 1991-12-13 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1994-12-12 1995-06-13 1995-12-13 $7700.00 Window Closed / Lapsed

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