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US4626554A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for producing modified styrenic polymer beads for high strength foamed articles

Assignee: Lyondell Chemical Technology LP
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Filing: 1985-11-29
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Granted: 1986-12-02
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Expires: 2005-11-29
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Abstract

Abstract Styrenic polymer beads that are useful in forming foamed cups with improved strength and thermal properties are prepared by forming an aqueous suspension of initial styrenic polymer beads and adding thereto an emulsion of a comonomer solution of styrenic monomer and divinylbenzene, which emulsion also contains free-radical-producing catalysts, and the suspension with added monomers is heated to copolymerize the styrenic monomer and divinylbenzene within and on the initial beads and form modified beads.

Inventors

  • 👤 Adolph V. DiGiulio

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 14:36
CPC Classifications
C; C08; C08J; C08J9/00; C08J9/16; C08J9/18; C08F; C08F257/00; C08F257/02; C08J2351/00; Y; Y10; Y10T; Y10T428/00; Y10T428/13; Y10T428/1352; Y10T428/1376; Y10T428/29; Y10T428/2982; Y10T428/2991; Y10T428/2998

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 268 words
A process for forming styrenic polymer beads modified with styrenic monomer/divinylbenzene copolymer for use in producing foamed cups with improved strength and thermal properties comprising: (a) forming an aqueous suspension of initial polystyrene beads having a weight average molecular weight of 230,000 to 350,000 with a polydispersity (Mw/Mn) of 2 to 3.1, with the aid of a suitable suspending agent system; (b) forming a comonomer solution of a styrene monomer and divinylbenzene; (c) forming an emulsion comprising a suitable emulsifier and said comonomer solution with free-radical-producing catalysts dissolved therein; (d) adding the emulsion to the styrene polymer bead suspension at 25°-75° C. to allow the comonomers and catalyst to be absorbed therein/thereon during the addition and shortly after the addition is complete, heating the resulting bead suspension to a polymerization temperature of about 80°-95° C., and maintaining said temperature for 0.10 to 6 hours to copolymerize said comonomers; and (e) heating said suspension to a temperature of 115° to about 135° C. to substantially complete the polymerization of said styrene monomer and divinylbenzene to form beads having copolymer diffused throughout but distributed primarily at or near the surface of the bead; (f) cooling the suspension to 105° C. or less; (g) adding a non-ionic surfactant and 3-12% by weight based on polymer of a blowing agent selected from the group consisting of aliphatic hydrocarbons containing 4 to 6 carbon atoms, halogenated hydrocarbons which boil at a temperature below the softening point of the polymer, and mixtures of these; (h) heating the suspension at a temperature of from 80°-150° C. to impregnate the polymer beads with blowing agent; and
Claim 2
Dependent Claim 268 words
A process for forming styrenic polymer beads modified with styrenic monomer/divinylbenzene copolymer for use in producing foamed cups with improved strength and thermal properties comprising: (a) forming an aqueous suspension of initial polystyrene beads having a weight average molecular weight of 230,000 to 350,000 with a polydispersity (Mw/Mn) of 2 to 3.1, with the aid of a suitable suspending agent system; (b) forming a comonomer solution of a styrene monomer and divinylbenzene; (c) forming an emulsion comprising a suitable emulsifier and said comonomer solution with free-radical-producing catalysts dissolved therein; (d) adding the emulsion to the styrene polymer bead suspension at 25°-75° C. to allow the comonomers and catalyst to be absorbed therein/thereon during the addition and shortly after the addition is complete, heating the resulting bead suspension to a polymerization temperature of about 80°-95° C., and maintaining said temperature for 0.10 to 6 hours to copolymerize said comonomers; and (e) heating said suspension to a temperature of 115° to about 135° C. to substantially complete the polymerization of said styrene monomer and divinylbenzene to form beads having copolymer diffused throughout but distributed primarily at or near the surface of the bead; (f) cooling the suspension to 105° C. or less; (g) adding a non-ionic surfactant and 3-12% by weight based on polymer of a blowing agent selected from the group consisting of aliphatic hydrocarbons containing 4 to 6 carbon atoms, halogenated hydrocarbons which boil at a temperature below the softening point of the polymer, and mixtures of these; (h) heating the suspension at a temperature of from 80°-150° C. to impregnate the polymer beads with blowing agent; and
Claim 3
Dependent Claim 19 words
(i) cooling the suspension to room temperature, acidifying the suspension, and separating the impregnated beads from the aqueous system.
Claim 4
Dependent Claim 19 words
(i) cooling the suspension to room temperature, acidifying the suspension, and separating the impregnated beads from the aqueous system.
Claim 5
Dependent Claim 30 words
The process of claim 1 wherein said suitable suspending agent system is tricalcium phosphate suspending agent in combination with sodium dodecylbenzene sulfonate surfactant and polyoxyethylene (20) sorbitan monolaurate non-ionic surfactant.
Claim 6
Dependent Claim 104 words
Expandable styrenic polymer beads for use in producing foamed cups with improved strength and thermal properties comprising (a) styrene polymer beads having 8-35% by weight of a copolymer of 99.15-99.98% by weight of styrenic monomer and 0.02-0.85% by weight of divinylbenzene diffused throughout but distributed primarily at or near the surface of said beads wherein said styrene polymer beads are produced by the process of claim 1, and (b) 3-12% of a blowing agent selected from the group consisting of aliphatic hydrocarbons containing 4-6 carbon atoms, halogenated hydrocarbons which boil at a temperature below the softening point of the polymer, and mixtures of these.

References Cited (Backward Citations)

US3324052A Cited
US3259595A Cited
US3259594A Cited
US3960784A Cited
US4579872A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1989-12-01 1990-06-02 1990-12-02 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1993-12-01 1994-06-02 1994-12-02 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1997-12-01 1998-06-02 1998-12-02 $7700.00 Window Closed / Lapsed

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