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US4085169A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for preparing styrenic polymer particles

Assignee: Sekisui Kaseihin Kogyo KK
•
Filing: 1975-09-29
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Granted: 1978-04-18
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Expires: 1995-09-29
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Abstract

Abstract Styrenic polymer particles having a substantially uniform particle size are prepared by suspending styrenic polymer particles having particle sizes in a certain range in water to provide an aqueous suspension and after adding to the suspension a styrenic monomer, a suspension polymerization catalyst and a polymerization retarder in an amount of 1/200 to 1/15 mole per 1 mole of the catalyst, conducting the suspension polymerization. By conducting the polymerization in the presence of a foaming agent, one can produce foamable styrenic polymer particles having a substantially uniform particle size.

Inventors

  • 👤 Fumio Saito
  • 👤 Fumito Yamai
  • 👤 Yositugu Beppu
  • 👤 Shinpei Nakayama

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 22:10
CPC Classifications
C; C08; C08F; C08F257/00; C08F257/02

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 340 words
A process for reducing the amount of powdery polymer particles which pass through a 32 mesh sieve to thereby obtain styrenic polymer particles having a uniform particle size of 0.6 to 3 mm by preparing styrenic polymer particles by the suspension polymerization of a system comprising styrenic monomer droplets and styrenic polymer particles using the styrenic monomer and styrenic polymer particles as raw materials, which comprises suspending styrene homopolymer particles or copolymer particles of styrene monomer and up to 50% by weight of a different copolymerizable ester monomer comprising an alkyl alcohol having from 1 to 12 carbon atoms and being selected from the group consisting of acrylic esters, methacrylic esters, maleic esters and fumaric esters, having particle sizes of 0.4 to 1.8 mm in water containing a suspending agent selected from the group consisting of a water-soluble high molecular weight material and a slightly soluble inorganic material and adding to the suspension styrene monomer with up to 50% by weight of a different copolymerizable monomer selected from the group consisting of methylacrylate, ethylacrylate, butylacrylate, methylmethacrylate, ethylmethacrylate, dimethylmaleate, diethylmaleate, acrylonitrile, α-methylstyrene, divinylbenzene and mixtures thereof, a suspension polymerization catalyst, and a polymerization retarder which is soluble in the styrene monomer and which has a molecular weight of at least 200, said retarder being selected from the group consisting of 3,5-di-tertiary butyl-4-hydroxytoluene, 1,1-bis(4-hydroxy-phenyl) cyclohexane, 4,4'-butylidene-bis(3-methyl-6-tertiary butyl phenol), 1,3,5-trimethyl-2,4,6-tris-3,5-di-tertiary-butyl-4-hydroxybenzylbenzene, 2,2'-methylenebis (6-tertiary-butyl-4-methylphenol, dilaurylthiodipropionate, 4,4'-thiobis (3-methyl-6-tertiary-butylphenol), N,N'-di-β-naphthyl-p-phenylenediamine, and N-phenyl-N-isopropyl-p-phenylenediamine in an amount of 1/100 to 1/25 mol per mol of said suspension polymerization catalyst to conduct the polymerization of said styrenic monomer while absorbed in said polymer particles, whereby the size of said polymer particles is increased, said polymerization retarder retarding the polymerization of said styrenic monomer droplets until said styrenic monomer is absorbed by said polymer particles, the amount of said polymer and said monomer used as raw material being 5 to 60 weight % and 95 to 40 weight %, respectively, of the polymer particles produced, to thereby obtain sytrenic polymer particles having a uniform particle size of 0.6 to 3 mm.
Claim 2
Dependent Claim 340 words
A process for reducing the amount of powdery polymer particles which pass through a 32 mesh sieve to thereby obtain styrenic polymer particles having a uniform particle size of 0.6 to 3 mm by preparing styrenic polymer particles by the suspension polymerization of a system comprising styrenic monomer droplets and styrenic polymer particles using the styrenic monomer and styrenic polymer particles as raw materials, which comprises suspending styrene homopolymer particles or copolymer particles of styrene monomer and up to 50% by weight of a different copolymerizable ester monomer comprising an alkyl alcohol having from 1 to 12 carbon atoms and being selected from the group consisting of acrylic esters, methacrylic esters, maleic esters and fumaric esters, having particle sizes of 0.4 to 1.8 mm in water containing a suspending agent selected from the group consisting of a water-soluble high molecular weight material and a slightly soluble inorganic material and adding to the suspension styrene monomer with up to 50% by weight of a different copolymerizable monomer selected from the group consisting of methylacrylate, ethylacrylate, butylacrylate, methylmethacrylate, ethylmethacrylate, dimethylmaleate, diethylmaleate, acrylonitrile, α-methylstyrene, divinylbenzene and mixtures thereof, a suspension polymerization catalyst, and a polymerization retarder which is soluble in the styrene monomer and which has a molecular weight of at least 200, said retarder being selected from the group consisting of 3,5-di-tertiary butyl-4-hydroxytoluene, 1,1-bis(4-hydroxy-phenyl) cyclohexane, 4,4'-butylidene-bis(3-methyl-6-tertiary butyl phenol), 1,3,5-trimethyl-2,4,6-tris-3,5-di-tertiary-butyl-4-hydroxybenzylbenzene, 2,2'-methylenebis (6-tertiary-butyl-4-methylphenol, dilaurylthiodipropionate, 4,4'-thiobis (3-methyl-6-tertiary-butylphenol), N,N'-di-β-naphthyl-p-phenylenediamine, and N-phenyl-N-isopropyl-p-phenylenediamine in an amount of 1/100 to 1/25 mol per mol of said suspension polymerization catalyst to conduct the polymerization of said styrenic monomer while absorbed in said polymer particles, whereby the size of said polymer particles is increased, said polymerization retarder retarding the polymerization of said styrenic monomer droplets until said styrenic monomer is absorbed by said polymer particles, the amount of said polymer and said monomer used as raw material being 5 to 60 weight % and 95 to 40 weight %, respectively, of the polymer particles produced, to thereby obtain sytrenic polymer particles having a uniform particle size of 0.6 to 3 mm.
Claim 3
Dependent Claim 27 words
The process of claim 1 wherein the weight ratio of styrenic monomer to styrenic polymer particles as raw materials is 95 : 5 to 60 : 40.
Claim 4
Dependent Claim 57 words
The process of claim 1 wherein the styrenic polymer particles as raw materials have a mesh size defined by d max = n x d min , wherein 1 < n ≦ 3, where d max is the mesh size of the largest polymer particles and d min is the mesh size of the smallest polymer particles.
Claim 5
Dependent Claim 11 words
The process of claim 2 wherein 1 < n ≦ 1.5.
Claim 6
Dependent Claim 26 words
The process of claim 1 wherein said polymerization retarder is selected from the group consisting of 3,5-di-tertiary, butyl-4-hydroxytoluene, 4,4'-butylidene bis (3-methyl-6-tertiary butyl phenol), N,N'-di-β-naphtyl-p-phenylenediamine and N-phenyl-N-isopropyl-p-phenylenediamine.
Claim 7
Dependent Claim 27 words
The process of claim 1 wherein the amount of powdery polymer particles which pass through a 32 mesh sieve is reduced to less than 1% by weight.

References Cited (Backward Citations)

US2934530A Cited
US3440219A Cited
US3423351A Cited
US3736273A Cited
US3696172A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-04-17 1981-10-17 1982-04-18 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-04-17 1985-10-17 1986-04-18 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-04-17 1989-10-17 1990-04-18 $7700.00 Window Closed / Lapsed

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