Process for producing prefoamed polymer particles

• US 4,464,484 A
• Filed: 12/13/1983
• Issued: 08/07/1984
• Est. Priority Date: 12/20/1982
• Status: Expired due to Term

• Current Assignee: Japan Styrene Paper Corporation
• Original Assignee: Japan Styrene Paper Corporation
• Inventors: Kuwabara, Hideki, Yoshimura, Shohei
• Primary Examiner(s): Foelak, Morton
• Application Number:
  US06/561,095
• Time in Patent Office: 238 Days
• Field of Search: 521/56, 521/60, 521/58, 264/53, 264/50, 264/DIG. 9, 264/DIG. 15
• US Class Current: 521/58
• CPC Class Codes: B29C 44/3461 Making or treating expandable particles
• CPC Class Codes: C08J 9/122 Hydrogen, oxygen, CO2, nitrogen or noble gases
• CPC Class Codes: C08J 9/18 by impregnating polymer particles with the blowing agent
• CPC Class Codes: C08J 9/228 Forming foamed products
• CPC Class Codes: Y10S 264/09 Pre-expansion of foamed polystyrene
• CPC Class Codes: Y10S 264/15 Aging of foamed resin products

Abstract

Prefoamed polymer particles having excellent moldability are produced by a process comprising a step (impregnating step) of impregnating carbon dioxide or carbon dioxide and a volatile blowing agent in polymer particles, a step (dispersing step) of dispersing the polymer particles into a dispersion medium in a sealed vessel, a step (heating step) of heating the polymer particles to a temperature higher than the softening point of said polymer particles, and a step (releasing step) of opening one end of said vessel and simultaneously releasing the polymer particles and dispersion medium from inside the vessel to an atmosphere held at a pressure lower than that of the vessel. In this process, the impregnating step, dispersing step and heating step need not be altogether effected separately. These steps can be performed simultaneously in one and the same vessel.

Claims

1. A process for producing prefoamed polymer particles, which comprises a step of impregnating carbon dioxide in polymer particles, a step of dispersing the polymer particles into a dispersion medium in a sealed vessel, a step of heating the polymer particles to a temperature higher than the softening point of said polymer particles, and a step of opening one end of said vessel and simultaneously releasing the polymer particles and dispersion medium from inside the vessel to an atmosphere held at a pressure lower than that of the vessel.

2. The process of claim 1 wherein 5 to 50 parts by weight of carbon dioxide per 100 parts by weight of the polymer particles is impregnated in the polymer particles.

6. The process of claim 1 or 3 wherein polymer particles made of a polyolefin resin are used.

7. The process of claim 1 or 3 wherein crystalline polymer particles are used and said particles are heated to a temperature in the range of from a temperature 10°

C. lower than the melting point of said polymer to a temperature 50°

C. higher than the melting point of said polymer.

8. The process of claim 1 or 3 wherein amorphous polymer particles are used and said particles are heated to a temperature in the range of from a temperature 10°

C. higher than the softening point of said polymer to a temperature 70°

C. higher than the softening point of said polymer.

9. The process of claim 1 or 3 wherein water, ethylene, glycol, glycerol, methanol or ethanol is used as the dispersion medium.

10. The process of claim 1 or 3 wherein the polymer particles and dispersion medium are released from inside a vessel held at 20 to 100 kg/cm² to an atmosphere held at atmospheric pressure.

3. A process for producing prefoamed polymer particles, which comprises a step of impregnating carbon dioxide and a volatile blowing agent in polymer particles, a step of dispersing the polymer particles into a dispersion medium in a sealed vessel, a step of heating the polymer particles to a temperature higher than the softening point of said polymer particles, and a step of opening one end of said vessel and simultaneously releasing the polymer particles and dispersion medium from inside the vessel to an atmosphere held at a pressure lower than that of the vessel.

4. The process of claim 3 wherein carbon dioxide and the volatile blowing agent in the total amount of 5 to 30 parts by weight per 100 parts by weight of the polymer particles are impregnated in the polymer particles.

5. The process of claim 3 wherein the volatile blowing agent is used in an amount of 20 to 800 parts by weight per 100 parts by weight of carbon dioxide.