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US4622346A 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: 1986-11-11
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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 2026-10-30 06:30
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

Claims Analysis

Total Claims: 4
Claim 1
Independent Claim 341 words
The process for forming styrene polymer beads having a styrene monomer-divinylbenzene copolymer relatively uniformly dispersed throughout the bead 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 styrene monomer and divinylbenzene; (c) forming an emulsion comprising suitable emulsifier and a portion of said comonomer solution; (d) adding the emulsion to the styrene polymer bead suspension at 25°-75° C. to allow the comonomers to be absorbed into the beads; (e) forming a second emulsion comprising a suitable emulsifier, the remaining portion of said comonomer solution, and free-radical-producing catalysts; (f) adding the second emulsion to the suspension of said beads absorbed with comonomers at 25°-75° C., at a rate such that the rate of absorption of comonomer/catalyst by said beads is at least equivalent to the rate of addition of emulsified comonomer/catalyst solution, then allowing said suspension to stand for 30 minutes to 4 hours, and then raising the temperature to 80°-95° C., and maintaining the suspension at said temperature to polymerize said comonomers; and (g) heating said suspension at a temperature of 115° C. to about 135° C. to substantially complete the polymerization of said styrene monomer and divinylbenzene to form beads having copolymer relatively uniformly distributed throughout the beads; (h) cooling the suspension to 105° C. or less; (i) 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; (j) heating the suspension at a temperature of from 80°-150° C. to impregnate the polymer beads with blowing agent; and (k) cooling the suspension to room temperature, acidifying the suspension, and separating the impregnated beads from the aqueous system.
Claim 2
Dependent Claim 341 words
The process for forming styrene polymer beads having a styrene monomer-divinylbenzene copolymer relatively uniformly dispersed throughout the bead 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 styrene monomer and divinylbenzene; (c) forming an emulsion comprising suitable emulsifier and a portion of said comonomer solution; (d) adding the emulsion to the styrene polymer bead suspension at 25°-75° C. to allow the comonomers to be absorbed into the beads; (e) forming a second emulsion comprising a suitable emulsifier, the remaining portion of said comonomer solution, and free-radical-producing catalysts; (f) adding the second emulsion to the suspension of said beads absorbed with comonomers at 25°-75° C., at a rate such that the rate of absorption of comonomer/catalyst by said beads is at least equivalent to the rate of addition of emulsified comonomer/catalyst solution, then allowing said suspension to stand for 30 minutes to 4 hours, and then raising the temperature to 80°-95° C., and maintaining the suspension at said temperature to polymerize said comonomers; and (g) heating said suspension at a temperature of 115° C. to about 135° C. to substantially complete the polymerization of said styrene monomer and divinylbenzene to form beads having copolymer relatively uniformly distributed throughout the beads; (h) cooling the suspension to 105° C. or less; (i) 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; (j) heating the suspension at a temperature of from 80°-150° C. to impregnate the polymer beads with blowing agent; and (k) cooling the suspension to room temperature, acidifying the suspension, and separating the impregnated beads from the aqueous system.
Claim 3
Dependent Claim 28 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 4
Dependent Claim 97 words
Expandable styrene 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 styrene monomer and 0.02-0.85% by weight of divinylbenzene relatively uniformly distributed throughout said beads, wherein said styrene polymer beads are prepared 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) 1989-11-10 1990-05-12 1990-11-11 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1993-11-10 1994-05-12 1994-11-11 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1997-11-10 1998-05-12 1998-11-11 $7700.00 Window Closed / Lapsed

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