Process for skin foam

• US 4,518,557 A
• Filed: 05/18/1981
• Issued: 05/21/1985
• Est. Priority Date: 05/18/1981
• Status: Expired due to Term

• Current Assignee: James River Paper Company, Inc.
• Original Assignee: James River-Norwalk Incorporated
• Inventors: Wecker, Sheldon M.
• Primary Examiner(s): Anderson, Philip
• Application Number:
  US06/264,574
• Time in Patent Office: 1,464 Days
• Field of Search: 264/45.9, 264/46.1, 264/51, 264/171, 425/115, 425/817 C
• US Class Current: 264/45.9
• CPC Class Codes: B29C 44/04 consisting of at least two parts of chemically or physically different materials, e.g. having different densities
• CPC Class Codes: B29C 44/22 consisting of at least two parts of chemically or physically different materials, e.g. having different densities
• CPC Class Codes: B29C 48/00 Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor extrusion blow-moulding B29C49/04
• CPC Class Codes: B29C 48/10 flexible, e.g. blown foils

Abstract

In the manufacture of skinned foam a technique for matching the viscosity of the skin as well as the foam so that both flow uniformly through the die includes the addition of blowing agent to all of the layers of the structure. To prevent foaming of the skin layers, nucleating agent is not added at those layers and the temperature is controlled so as to prevent nucleation without a nucleating agent. More specifically, the skins are kept above the boiling point of the blowing agent at atmospheric pressure and melt temperature, but below the temperature at which homogeneous nucleation occurs.

Claims

1. In a method of making a foamed plastic product having a relatively low density cellular core structure and a substantially non-cellular outer layer or skin wherein a first or foam stream of foamable normally solid molten polymer containing blowing agent is fed to a co-extrusion die under pressure and expanded on exiting from said die to form said cellular core and a second or skin stream of said normally solid molten polymer is supplied to said co-extrusion die to form said skin, the improvement which comprises:

incorporating a volatile organic blowing agent and a nucleating agent in said first or foam stream of polymer,

incorporating a volatile organic blowing agent in said second or skin stream of polymer in an amount effective to match the viscosity of said second stream to that of said first stream and maintain stable flow of said second stream relative to said first stream,

supplying said second stream to said co-extrusion die at a temperature sufficient to produce foam formation on expansion of the polymer leaving the die, and

supplying said second stream to said co-extrusion die at a temperature lower than that required to producing foaming in said second stream of polymer on release of pressure in said co-extrusion die.

2. The method of claim 1 wherein said volatile organic blowing agent is a chlorofluorocarbon.

6. The method of claim 1 wherein said polymer is a styrene resin.

7. The method of claim 1 wherein said volatile organic blowing agent is n-pentane.

8. The method of claim 2 wherein said blowing agent is dichlorodifluoromethane.

9. The method of claim 1 wherein said nucleating agent is a mixture of citric acid and sodium bicarbonate.

10. The method of claim 1 wherein said nucleating agent is SMA, a co-polymer of styrene and maleic anhydride.

11. The method of claim 1 wherein said nucleating agent is talc.

3. A method of making a foamed plastic product having a non-cellular outer surface or skin of relatively high density and a foamed core having a relatively low density cellular structure comprising:

feeding a first or foam stream of a foamable normally solid molten polymer containing a blowing agent and a nucleating agent under pressure to one outlet of a co-extrusion die where it is expanded to substantially atmospheric pressure with foaming a formation of said inner core structure;

feeding a second or skin stream of a foamable normally solid molten polymer containing a volatile organic liquid blowing agent in an amount effective to match the viscosity of said second stream to that of said first stream and maintain stable flow of said second stream relative to said first stream and free from any added nucleating agent to said co-extrusion die under pressure wherein it is extruded with said first stream of polymer;

supplying said first or foam stream to said co-extrusion die at a temperature sufficient to cause foaming of said polymer on release of pressure; and

supplying said second or skin stream to said co-extrusion die at a temperature below that at which foaming of said polymer occurs spontaneously on release of pressure thereby forming a skin on said foamed core.

4. A method according to claim 3 wherein said second stream is supplied to said co-extrusion die at points adjacent each side of said first stream forming a foamed sheet with a skin surface on each side of said core.

5. A process according to claim 3 wherein the polymer in each stream comprises a styrene resin and the blowing agent in each comprises a chlorofluorocarbon.