초록

This invention relates to a process of preparing vesiculated granules of crosslinked carboxylated polyester resin utilising a particular class of non-alkylphenolethoxylate surfactant.

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1. A process of preparing vesiculated granules of crosslinked carboxylated polyester resin, said process comprising the steps of:(a) forming a dispersion of particles of a solution in ethylenically unsaturated monomer of a carboxylated unsaturated polyester resin having an acid value of from 5-50mg

1. A process of preparing vesiculated granules of crosslinked carboxylated polyester resin, said process comprising the steps of:(a) forming a dispersion of particles of a solution in ethylenically unsaturated monomer of a carboxylated unsaturated polyester resin having an acid value of from 5-50mg KOh/g, th solution also containing water droplets which are dispersed in the presence of a base selected from:Ci) a water-soluble polyamine which contains at least three amine groups per molecule and which has a dissociation constant (pKa value) of 9.5-10.5; and(ii) a metal oxide, hydroxide or salt wherein the metal cation is chosen from the group consisting of calcium, magnesium, barium, titanium, zinc, lead, stroatium and cobalt, the salt being one wherein the pK a value of the conjugate acid of the anion is greater than 2;the dispersion additionally containing a surfactant which is free of alkylphenol moieties, and(b) initiating free radical polymerisation to cross-link the polyester and monomer and provide crosslinked, vesiculated granules, wherein:(i) where a water-soluble polyamine is used, there are present from 0.3-4.0 amine groups per polyester carboxyl group;(ii) where a metal oxide, hydroxide or salt is used, there is present from 0.8-1.8 equivalents of metal cation per equivalent of polyester carboxyl group; and(iii) the surfacant comprises a species of the formula (I) a H 2a+1 —O—(CH 2 CH 2 O) b SO 3 −   (1)where a is 6 to 12 and b is 2 to 8. 2. A process according to claim 1 wherein a is 8 to 11. 3. A process according to claim 1 wherein b is from 3 to 5. 4. A process according to claim 1 wherein the carboxylated unsaturated polyester resin is an unsaturated condensation product of a polybasic acid (or corresponding anhydride) and a dihydric alcohol. 5. A process according to claim 4 wherein the polybasic acid is selected from unsaturated aliphanic acids, saturated aliphatic acids and saturated aromatic acids. 6. A process according to claim 4 wherein the dihydric alcohol is selected from ethylene glycol, poly(ethylene glycols), and alcohols which contain three or more hydroxyl groups, the hydroxyl groups in excess of two optionally being at least in part etherified with a monohydric alcohol or esterified with a monobasic acid. 7. A process according to claim 1 wherein the ethylenically unsaturated monomer has a solubiliry of 20° C. of less than 5% (w/w) in water. 8. A process according to claim 1 wherein the ethylenically unsaturated monomer is a mixture of monomers. 9. A process according to claim 8 wherein the ethylenically unsaturated monomer includes a minor amount of a polyfunctional monomer. 10. A process according to claim 9 wherein the polyfunctional monomer is divinyl bernzene. 11. A process according to claim 1 wherein the ethylenically unsaturated monomer is selected from styrene, methyl styrene and methymethacrylate and mixtures thereof. 12. A process according to claim 8 wherein the ethylenicaily unsaturated monomer includes a minor amount of a comonomer selected from ethyl acrylate, n-butyl, methacrylate, acrylonitrile and triallyl cyanurate. 13. A process according to claim 1 wherein the surfactant is present in an amount of fron 0.75 to 7.5% by weight of dispersant solids per volume of total granule solids. 14. A process according to claim 1 wherein the surfactant has a counter ion selected from NH 4 + , Mg 2+ and K + . 15. A process according to claim 1 wherein the base is a polyamine base selected from diethylene triamine, triethylene tetramine and oligomers of vinyl pyridine or dimethylaminoethylmethacrylate with polyethylene glycol methacrylare or mixtures thereof. 16. A process according to claim 1 wherein the base is magnesium oxide. 17. A process according to claim 16 wherein the magnesium oxide is present such that there are 0.8 to 1.8 equivalents of metal cation per polyester carboxyl group. 18. A process according to claim 15 wherein the base is an amine base present in an amount such that there are present 0.3 to 4.0 amine groups per polyester carboxyl group. 19. A process according to claim 1 wherein the dispersion of particles of a solution in ethylenically unsaturated monomer of carboxylic unsaturated polyester resin is prepared by a double emulsion process in which water is emulsified into a solution in ethylenicailly unsaturated monomer of a carboxylated unsaturated polyester resin by mechanical agitation to form a first emulsion, which emulsion is dispersed in water in the presence of a stabiliser to form a double emulsion. 20. A process according to claim 19 wherein the stabiliser is a water soluble partially hydrolysed poly(vinyl acetate) with a molecular weight of about 100,000 and a degree of hydrolysis of 85-90%. 21. A process according to claim 19 wherein the first emulsion is dispersed in water in the presence of a water-soluble polymeric thickener. 22. A process according to claim 21 wherein the thickener is hydroxyethyl cellulose. 23. A process according to claim 22 wherein the concentration of hydroxymethyl cellulose is about 01 to 0.5% by weight of the continuous phase of the double emulsion. 24. A process according to claim 1 wherein the free radical polymerisation is initiated by the use of a free radical initiator or by exposure to a radiation source. 25. A process according to claim 24 wherein the polymerisation is initiated by a redox system of diethyl triamine and t-buryl perbenzoate triggered by ferrous ions derived from ferrous sulphate. 26. A process according to claim 19 wherein the double emulsion is prepared at room temperature and raised to a temperature of between 35° C. and 40° C. prior to addition of a free radical polymerisation initiator. 27. A process according to claim 19 wherein the double emulsion is raised to a temperature of about 50° C. prior to addition of a free radical polymerisation initiator. 28. A process according to claim 1 wherein the polymerisation is preformed under a nitrogen blanket.