Claims
- 1. A stable dispersion of addition (co)polymers in an inert relatively non-polar organic hydrocarbon liquid, the dispersed particles embracing both a (co)polymer and a polymer containing an ethylenically unsaturated monomer, characterized in that the (co)polymers are substantially composed of:
- a. 5 to 100 mole % of styrene and/or methyl styrene; and
- b. 0 to 95 mole % of alkyl methacrylate having 1 or 2 carbon atoms in the alkyl group and/or alkoxyalkylene methacrylate having 1 or 2 carbon atoms in the alkoxy group and the alkylene group;
- and that they are grafted to a non-functionalized polymer of a number average molecular weight of 2,000 to 10,000, at least 60% by weight of which consists of butadiene, the weight percentage of the butadiene-containing polymer being 20 to 200% of that of the (co)polymer and the sum of this percentage and the percentage styrene and/or methyl styrene in the copolymer being higher than or equal to 50, said dispersion containing solid particles having a number average molecular weight in the range of 60,000 to 1,000,000 which dispersion dry at room temperature to yield essentially a smooth film having a high gloss.
- 2. A dispersion according to claim 1, characterized in that the weight ratio between the (co)polymers and the butadiene-containing polymer is in the range of 4:1 to 1:2.
- 3. A dispersion according to claim 1, characterized in that the butadiene-containing polymer is composed of butadiene, styrene and/or acrylonitrile.
- 4. A dispersion according to claim 1, characterized in that it contains a drier, such as the octoate or naphthenate of Co, Ce, Fe, Cu, Mn, Zr, Ca, Ba and/or Pb.
- 5. A dispersion according to claim 1, characterized in that it contains a pigment in an amount of at least 5% by weight, based on the addition (co)polymers.
- 6. A dispersion according to claim 5, characterized in that as pigment non-leafing aluminum is used.
- 7. A process for the preparation of a stable dispersion according to claim 1, characterized in that a composition substantially consisting of:
- a. 5 to 100 mole % of styrene and/or methyl styrene; and
- b. 0 to 95 mole % of alkyl methacrylate with 1 or 2 carbon atoms in the alkyl group and/or alkoxyalkylene methacrylate with 1 or 2 carbon atoms in the alkoxy group and the alkylene group;
- together with an active amount of a peroxide as initiator is polymerized in an inert relatively non-polar organic hydrocarbon liquid at a temperature of 60.degree. C. to 120.degree. C. in the presence of non-functionalized polymer containing at least 60% by weight of butadiene and having a number average molecular weight in the range of 2,000 to 10,000, the weight percentage of the butadiene-containing polymer being 20 to 200 % of that of the (co)polymer and the sum of this percentage and the percentage styrene and/or methyl styrene in the copolymer being higher than or equal to 50.
- 8. A process according to claim 7, characterized in that the weight ratio between the (co)polymer and the butadiene-containing polymer is in the range of 4:1 to 1:2.
- 9. A process according to claim 7, characterized in that the polymerization is carried out in an inert relatively non-polar organic hydrocarbon liquid which is a non-solvent for polystyrene and/or polymethyl styrene and/or styrene-methacrylate copolymers and/or styrene methacrylate methacrylic acid copolymers and/or methyl styrene-methacrylate copolymers and/or methyl styrene-methacrylate-methacrylic acid copolymers and a solvent for the butadiene-containing polymer.
- 10. A process according to claim 7, characterized in that the inert relatively non-polar organic hydrocarbon liquid contains at least 50 % by weight of aliphatic hydrocarbons.
- 11. A process according to claim 7, characterized in that the polymerization is carried out in turpentine, white spirit, petroleum ether or iso-octane.
- 12. A process according to claim 7, characterized in that the polymerization is carried out using as initiator a substituted or unsubstituted dibenzoyl peroxide in an amount of 0.1 to 10% by weight, calculated on the butadiene-containing polymer.
- 13. A process according to claim 7, characterized in that the polymerization is carried out using as initiator a substituted or unsubstituted dibenzoyl peroxde in an amount of 1 to 5% by weight, calculated on the butadiene-containing polymer.
- 14. A process according to claim 12, or 13, characterized in that as substituted dibenzoyl peroxide there is used di(ortho-methylbenzoyl)peroxide and/or di(2,4-dichlorobenzoyl)peroxide.
- 15. A process according to claim 7, characterized in that the polymerization is carried out at a temperature in the range of 80.degree. to 100.degree. C.
- 16. A process for coating a substrate of wood, plastics or a metal, characterized in that a dispersion according to claim 1 is applied to the substrate and cured.
Priority Claims (1)
Number |
Date |
Country |
Kind |
8402305 |
Jul 1984 |
NLX |
|
Parent Case Info
This application is a continuation of application Ser. No. 756,258, filed July 18, 1985, now abandoned.
US Referenced Citations (5)
Foreign Referenced Citations (6)
Number |
Date |
Country |
2157886 |
Jun 1971 |
DEX |
2259838 |
Aug 1975 |
FRX |
0030894 |
Mar 1976 |
JPX |
893429 |
Apr 1962 |
GBX |
990154 |
Apr 1965 |
GBX |
1011482 |
Dec 1965 |
GBX |
Non-Patent Literature Citations (1)
Entry |
Chemical Abstrcts, vol. 91, No. 22, Nov. 1979, p. 77, No. 176794e, Columbus Ohio, U.S.; and JP-A-79 71 126 (Hitachi Chemical Co., Ltd.) 07-06-1979. |
Continuations (1)
|
Number |
Date |
Country |
Parent |
756258 |
Jul 1985 |
|