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US4371636A
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Preparation of copolymer dispersions having a narrow particle size distribution, and exhibiting dilatant flow over a broad range of concentrations
Assignee: BASF SE
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Filing: 1981-07-01
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Granted: 1983-02-01
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Expires: 2001-07-01
Abstract
Abstract A process for the preparation of copolymer dispersions having a narrow particle size distribution, and exhibiting dilatant flow over a broad range of concentrations, by emulsion copolymerization of from 1 to 10% by weight, based on total monomers, of α,β-monoolefinically unsaturated monocarboxylic acids and/or dicarboxylic acids with other monoolefinically unsaturated monomers and with from 0 to 5% by weight of polyolefinically unsaturated monomers in the presence of conventional emulsifiers, dispersants and polymerization initiators, and in the presence or absence of regulators, wherein the monomers are copolymerized in aqueous emulsion, with simultaneous agglomeration but only partial fusion of the initially formed polymer particles, at a temperature near the glass transition temperature of the copolymer formed, and thereafter (A) the copolymer content of the aqueous copolymer dispersion is brought to 35-55% by weight and the pH to 3-5 or (B) the water contained in the aqueous copolymer dispersion is entirely or partially replaced by a water-miscible liquid which does not dissolve or swell the copolymer.
Inventors
- 👤 Dieter Distler
- 👤 Hans Wolf
- 👤 Gerhard Welzel
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-27 23:11
CPC Classifications
C; C08; C08F; C08F220/00; C08F220/02; C08F220/10; C08F220/12; C08J; C08J3/00; C08J3/02; C08J3/09
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
212 words
A process for the preparation of copolymer dispersions having a narrow particle size distribution, and exhibiting dilatant flow over a broad range of concentrations, which comprises emulsion copolymerization of (a) from 2 to 10% by weight, based on total monomers, of a,b-monoolefinically unsaturated monocarboxylic acids or dicarboxcylic acids (b) from 0 to 98% by weight of acrylic acid esters or methacrylic acid esters of alkanols of 1 to 4 carbon atoms, (c) from 0 to 98% by weight of styrene or methyl methacrylate; and (d) from 0 to 3% by weight of polyolefinically unsaturated monomers; the amount of the monomers (b) and (c) together being from 90 to 98% by weight, at 60°-95° C., in the presence of from 0 to 0.5% by weight of an anionic emulsifier and from 0 to 1% by weight of a non-ionic emulsifier, the percentages being based on the weight of monomers, with simultaneous agglomeration but only partial fusion of the initially formed polymer particles, which have a diameter of from 5 to 200 nm, at a temperature of ±10° C. of the glass transition temperature of the copolymer formed, and thereafter adjusting the copolymer content of the aqueous copolymer dispersion formed to 35-55% by weight and the pH to 3.8-5.0, unless these values already obtain.
Claim 2
Dependent Claim
212 words
A process for the preparation of copolymer dispersions having a narrow particle size distribution, and exhibiting dilatant flow over a broad range of concentrations, which comprises emulsion copolymerization of (a) from 2 to 10% by weight, based on total monomers, of a,b-monoolefinically unsaturated monocarboxylic acids or dicarboxcylic acids (b) from 0 to 98% by weight of acrylic acid esters or methacrylic acid esters of alkanols of 1 to 4 carbon atoms, (c) from 0 to 98% by weight of styrene or methyl methacrylate; and (d) from 0 to 3% by weight of polyolefinically unsaturated monomers; the amount of the monomers (b) and (c) together being from 90 to 98% by weight, at 60°-95° C., in the presence of from 0 to 0.5% by weight of an anionic emulsifier and from 0 to 1% by weight of a non-ionic emulsifier, the percentages being based on the weight of monomers, with simultaneous agglomeration but only partial fusion of the initially formed polymer particles, which have a diameter of from 5 to 200 nm, at a temperature of ±10° C. of the glass transition temperature of the copolymer formed, and thereafter adjusting the copolymer content of the aqueous copolymer dispersion formed to 35-55% by weight and the pH to 3.8-5.0, unless these values already obtain.
Claim 3
Dependent Claim
212 words
A process for the preparation of copolymer dispersions having a narrow particle size distribution, and exhibiting dilatant flow over a broad range of concentrations, which comprises copolymerization of (a) from 2 to 10% by weight, based on total monomers, of a,b-monoolefinically unsaturated monocarboxylic acids or dicarboxylic acids (b) from 0 to 98% by weight of acrylic acid esters or methacrylic acid esters of alkanols of 1 to 4 carbon atoms, (c) from 0 to 98% by weight of styrene or methyl methacrylate; and (d) from 0 to 3% by weight of polyolefinically unsaturated monomers; the amount of the monomers (b) and (c) together being from 90 to 98% by weight, at 60°-95° C., in the presence of from 0 to 0.5% by weight of an anionic emulsifier and from 0 to 1% by weight of a non-ionic emulsifier, the percentages being based on the weight of monomers, with simultaneous agglomeration but only partial fusion of the initially formed polymer particles, which have a diameter of from 5 to 200 nm, at a temperature of ±10° C. of the glass transition temperature of the copolymer formed, and thereafter entirely or partially replacing the water contained in the aqueous copolymer dispersion formed by a water-miscible liquid which does not dissolve or swell the copolymer.
Claim 4
Dependent Claim
212 words
A process for the preparation of copolymer dispersions having a narrow particle size distribution, and exhibiting dilatant flow over a broad range of concentrations, which comprises copolymerization of (a) from 2 to 10% by weight, based on total monomers, of a,b-monoolefinically unsaturated monocarboxylic acids or dicarboxylic acids (b) from 0 to 98% by weight of acrylic acid esters or methacrylic acid esters of alkanols of 1 to 4 carbon atoms, (c) from 0 to 98% by weight of styrene or methyl methacrylate; and (d) from 0 to 3% by weight of polyolefinically unsaturated monomers; the amount of the monomers (b) and (c) together being from 90 to 98% by weight, at 60°-95° C., in the presence of from 0 to 0.5% by weight of an anionic emulsifier and from 0 to 1% by weight of a non-ionic emulsifier, the percentages being based on the weight of monomers, with simultaneous agglomeration but only partial fusion of the initially formed polymer particles, which have a diameter of from 5 to 200 nm, at a temperature of ±10° C. of the glass transition temperature of the copolymer formed, and thereafter entirely or partially replacing the water contained in the aqueous copolymer dispersion formed by a water-miscible liquid which does not dissolve or swell the copolymer.
Claim 5
Dependent Claim
28 words
A copolymer dispersion having a narrow particle size distribution and exhibiting dilatant flow over a broad range of concentrations prepared by the processes of claim 1 or 2.
Claim 6
Dependent Claim
30 words
The dilatant copolymer dispersions of claim 3 wherein the ratio of the weight average of the particles to the number average is in the range of from 1 to 1.2.
Claim 7
Dependent Claim
19 words
The dilatant copolymer dispersion of claim 3 wherein said copolymer has a glass transition temperature of above 50° C.
Claim 8
Dependent Claim
28 words
The dilatant copolymer dispersion of claim 3 wherein the range of critical shearing rates of the copolymer of the dispersion ranges from 0.5 to 500 sec -1 .
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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) | 1986-01-31 | 1986-08-02 | 1987-02-01 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1990-01-31 | 1990-08-02 | 1991-02-01 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1994-01-31 | 1994-08-02 | 1995-02-01 | $7700.00 | Window Closed / Lapsed |