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US4168353A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for producing foamable polyethylene resin particles

Assignee: Sekisui Kaseihin Kogyo KK
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Filing: 1978-02-08
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Granted: 1979-09-18
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Expires: 1998-02-08
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Abstract

Abstract A process for producing foamable polyethylene resin particles which comprises suspending in an aqueous medium polyethylene resin particles having an MI value of 0.3 to 10, a density of less than 0.93 g/cm 3 and a softening point below 90° C., adding to the suspension 30 to 300% by weight based on the weight of the particles of a styrene monomer and a catalyst for polymerizing the monomer, polymerizing the monomer, and impregnating a blowing agent in the polyethylene resin particles containing the polymerized styrene resin to form foamable polyethylene resin particles.

Inventors

  • 👤 Yoshiaki Kitamori

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-27 07:11
CPC Classifications
C; C08; C08J; C08J9/00; C08J9/16; C08J9/18; C08J2351/00; C08J2351/06

Claims Analysis

Total Claims: 10
Claim 1
Independent Claim 166 words
A process for producing foamable polyethylene resin particles which comprises the steps of: (a) suspending in an aqueous medium polyethylene resin particles having an MI value of 0.3 to 10, a density of less than 0.93 g/cm 3 and a softening point below 90° C.; (b) adding to said aqueous suspension 30 to 300% by weight based on the weight of said particles of a styrene monomer and a catalyst for polymerizing said monomer; (c) polymerizing said monomer in the interior of said polyethylene resin particles; and (d) impregnating, after the polymerization, a blowing agent into the resulting polyethylene resin particles which contain a polystyrene resin formed by the polymerization of said styrene monomer at a temperature below the softening point of said polyethylene resin particles, wherein said blowing agent does not substantially reduce the viscosity of the polymerization system, does not dissolve said resin particles or only slightly swells the polyethylene resin particles, said polyethylene resin particles exhibiting excellent foaming ability and blowing agent retention.
Claim 2
Dependent Claim 166 words
A process for producing foamable polyethylene resin particles which comprises the steps of: (a) suspending in an aqueous medium polyethylene resin particles having an MI value of 0.3 to 10, a density of less than 0.93 g/cm 3 and a softening point below 90° C.; (b) adding to said aqueous suspension 30 to 300% by weight based on the weight of said particles of a styrene monomer and a catalyst for polymerizing said monomer; (c) polymerizing said monomer in the interior of said polyethylene resin particles; and (d) impregnating, after the polymerization, a blowing agent into the resulting polyethylene resin particles which contain a polystyrene resin formed by the polymerization of said styrene monomer at a temperature below the softening point of said polyethylene resin particles, wherein said blowing agent does not substantially reduce the viscosity of the polymerization system, does not dissolve said resin particles or only slightly swells the polyethylene resin particles, said polyethylene resin particles exhibiting excellent foaming ability and blowing agent retention.
Claim 3
Dependent Claim 43 words
The process for producing foamable polyethylene resin particles of claim 1, wherein said polyethylene resin is an ethylene homopolymer or copolymer containing ethylene as a major component with a monomer selected from the group consisting of vinyl chloride, vinyl acetate and methyl methacrylate.
Claim 4
Dependent Claim 46 words
The process for producing foamable polyethylene resin particles of claim 1, wherein said styrene monomer is styrene or a mixture of a major amount of styrene and a copolymerizable monomer selected from the group consisting of α-methyl styrene, acrylonitrile, methyl methacrylate, dimethyl maleate and divinyl benzene.
Claim 5
Dependent Claim 19 words
The process for producing foamable polyethylene resin particles of claim 1, wherein said aqueous medium contains a suspending agent.
Claim 6
Dependent Claim 22 words
The process for producing foamable polyethylene resin particles of claim 1, wherein said catalyst is an organic peroxide or an azo compound.
Claim 7
Dependent Claim 26 words
The process for producing foamable polyethylene resin particles of claim 1, wherein said blowing agent is an aliphatic hydrocarbon, a cycloaliphatic hydrocarbon, or a halogenated hydrocarbon.
Claim 8
Dependent Claim 37 words
The process for producing foamable polyethylene resin particles of claim 1, wherein said blowing agent is present in an amount of about 5 to 20% by weight based on the weight of the foamable polyethylene resin particles.
Claim 9
Dependent Claim 26 words
The process for producing foamable polyethylene resin particles of claim 1, wherein said polymerizing is at a temperature of from about 80° C. to 120° C.
Claim 10
Dependent Claim 47 words
The process for producing foamable polyethylene resin particles of claim 1, wherein said aqueous medium polyethylene resin particles have a softening point below 85° C. and said styrene monomer is added in an amount of 30 to 100% by weight based on the weight of said particles

References Cited (Backward Citations)

US3651183A Cited
US3413244A Cited
US3959189A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1982-09-17 1983-03-19 1983-09-18 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1986-09-17 1987-03-19 1987-09-18 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1990-09-17 1991-03-19 1991-09-18 $7700.00 Window Closed / Lapsed

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