US4169828A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Bead size distribution in the suspension polymerization of vinyl aromatic monomers
Assignee: Atlantic Richfield Co
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Filing: 1977-12-27
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Granted: 1979-10-02
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Expires: 1997-12-27
Abstract
Abstract The production of polymer beads by a suspension polymerization process in which a vinyl aromatic monomer having a free-radical generating catalyst dissolved therein is suspended in an aqueous medium with the aid of from 0.1 to 2.0 percent by weight, based on monomer, of a finely divided phosphate suspending agent in the presence of a modifier and heated to cause the monomer to polymerize into polymer beads is improved by the addition to the suspension of at least about 0.01 percent by weight based on monomer of an adjunct modifier, such as certain aminoalkanecarboxylic acids and N-substituted derivatives thereof. The process of the invention is especially applicable in the preparation of large polymer beads.
Inventors
- 👤 Harold A. Wright
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 16:20
CPC Classifications
C; C08; C08F; C08F12/00; C08F12/02; C08F12/04; Y; Y10; Y10S; Y10S526/00; Y10S526/909; Y10S526/91
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
121 words
In a process for producing polymer beads by suspending a vinyl aromatic monomer selected from the group consisting of styrene, alphamethylstyrene, monochlorostyrene and dichlorostyrene containing a monomer-soluble, free-radical producing catalyst in an aqueous medium with the aid of from 0.1 to 2.0 percent by weight based on monomer of a finely divided, difficultly water-soluble phosphate suspending agent and a bisulfite or persulfate modifier and subjecting the suspension to an elevated temperature to cause said monomer to polymerize, the improvement for producing a narrow distribution of bead diameter sizes which comprises adding to said suspension at least 0.01 percent by weight based on monomer of an adjunct modifier selected from the group consisting of glycine, β-alanine, N,N-bis-(2-hydroxyethyl) glycine, and N-tris-(hydroxymethyl) methyl glycine.
Claim 2
Dependent Claim
121 words
In a process for producing polymer beads by suspending a vinyl aromatic monomer selected from the group consisting of styrene, alphamethylstyrene, monochlorostyrene and dichlorostyrene containing a monomer-soluble, free-radical producing catalyst in an aqueous medium with the aid of from 0.1 to 2.0 percent by weight based on monomer of a finely divided, difficultly water-soluble phosphate suspending agent and a bisulfite or persulfate modifier and subjecting the suspension to an elevated temperature to cause said monomer to polymerize, the improvement for producing a narrow distribution of bead diameter sizes which comprises adding to said suspension at least 0.01 percent by weight based on monomer of an adjunct modifier selected from the group consisting of glycine, β-alanine, N,N-bis-(2-hydroxyethyl) glycine, and N-tris-(hydroxymethyl) methyl glycine.
Claim 3
Dependent Claim
20 words
The process of claim 1 wherein said polymerization produces polymer beads having an average particle size greater than 600 microns.
Claim 4
Dependent Claim
19 words
The process of claim 1 wherein said monomer is styrene and said catalyst comprises benzoyl peroxide and t-butyl perbenzoate.
Claim 5
Dependent Claim
11 words
The process of claim 1 wherein said phosphate is tricalcium phosphate.
Claim 6
Dependent Claim
115 words
In a process for producing polymer beads by suspending a vinyl aromatic monomer selected from the group consisting of styrene, alphamethylstyrene, monochlorostyrene, and dichlorostyrene containing a monomer-soluble, free-radical producing catalyst in an aqueous medium with the aid of from 0.1 to 2.0 percent by weight based on monomer of a finely divided, difficultly water-soluble phosphate suspending agent and subjecting the suspension to an elevated temperature to cause said monomer to polymerize, the improvement for producing a narrow distribution of bead diameter sizes which comprises adding to said suspension at least 0.01 percent by weight based on monomer of a sole modifier selected from the group consisting of glycine, β-alanine, N,N-bis-(2-hydroxyethyl) glycine, and N-tris-(hydroxymethyl) methyl glycine.
Claim 7
Dependent Claim
115 words
In a process for producing polymer beads by suspending a vinyl aromatic monomer selected from the group consisting of styrene, alphamethylstyrene, monochlorostyrene, and dichlorostyrene containing a monomer-soluble, free-radical producing catalyst in an aqueous medium with the aid of from 0.1 to 2.0 percent by weight based on monomer of a finely divided, difficultly water-soluble phosphate suspending agent and subjecting the suspension to an elevated temperature to cause said monomer to polymerize, the improvement for producing a narrow distribution of bead diameter sizes which comprises adding to said suspension at least 0.01 percent by weight based on monomer of a sole modifier selected from the group consisting of glycine, β-alanine, N,N-bis-(2-hydroxyethyl) glycine, and N-tris-(hydroxymethyl) methyl glycine.
Claim 8
Dependent Claim
68 words
The process of claim 1 wherein said vinyl aromatic monomer is copolymerized with a monomer selected from the group consisting of divinylbenzene, an alkyl acrylate, allyl acrylate, an alkyl methacrylate, allyl methacrylate, a diallyl ester of a dibasic aliphatic acid, a diallyl ester of a dibasic aromatic acid, butadiene, and polymers capable of further polymerization selected from the group consisting of styrene-butadiene rubbers, styrene-isoprene rubbers, and polybutadiene rubbers.
Claim 9
Dependent Claim
68 words
The process of claim 5 wherein said vinyl aromatic monomer is copolymerized with a monomter selected from the group consisting of divinylbenzene, an alkyl acrylate, allyl acrylate, an alkyl methacrylate, allyl methacrylate, a diallyl ester of a dibasic aliphatic acid, a diallyl ester of a dibasic aromatic acid, butadiene, and polymers capable of further polymerization selected from the group consisting of styrene-butadiene rubbers, styrene-isoprene rubbers and polybutadiene rubbers.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1982-10-01 | 1983-04-02 | 1983-10-02 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1986-10-01 | 1987-04-02 | 1987-10-02 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1990-10-01 | 1991-04-02 | 1991-10-02 | $7700.00 | Window Closed / Lapsed |