Hydroxy unsaturated diesters and copolymers thereof

Claim 2

A copolymer capable of cross linking to provide a thermosetting system, characterised in that the copolymer consists of monomers of the following three classes, in the weight percentages given: (A) from 11% to 30% of an ester mixture consisting of at least 70% by weight of an unsaturated diester of formula (I) r.sub.1 --o.sub.2 --ch═ch--c0.sub.2 --r.sub.2 (i) wherein: R 1 represents (a) a monohydroxy alkyl group of two to six carbon atoms; or (b) a 2,3-dihydroxypropyl group; or (c) a group of the empirical formula (I) --(ch.sub.2).sub.n O].sub.m [--(CH.sub.2).sub.x --OH (II) in which formula n=2 or 3; x=2 or 3, and m is from 1 to 800; and R 2 represents a linear or branched primary alkyl group having from 4 to 12 carbon atoms; which ester mixture has been prepared by reacting together 1.0 mole of a polyol of formula R 1 OH, 1.1 moles of a primary alcohol of formula R 2 OH and 1 mole of an acid of formula HO 2 C--CH═CH--CO 2 H, or 1 mole of the anhydride thereof, in the presence of para-toluene sulphonic acid as catalyst; (B) from 2% to 35% of an alkyl acrylate, having up to eight carbon atoms in the alkyl group, which group may be of linear or branched configuration; and (C) from 35% to 87% of at least one other monomer containing olefinic unsaturation, and chosen from the group consisting of methyl methacrylate, acrylic acid, vinyl acetate, and styrene.

Claim 3

Copolymer according to claim 1 characterised in that the unsaturated diester used is the reaction product of one of the following combinations of reactants: (i) isobutanol, ethylene glycol, and maleic acid or anhydride; (ii) butanol, ethylene glycol, and maleic acid or anhydride; (iii) 2-ethylhexanol, ethylene glycol, and maleic acid or anhydride; (iv) isobutanol, 1,2-propylene glycol, and maleic acid or anhydride; (v) isobutanol, glycerol, and maleic acid or anhydride; (vi) isobutanol, ethylene glycol, and fumaric acid.

Claim 4

Copolymer as claimed in claim 1 characterised in that the alkyl acrylate is chosen from butylacrylate or 2-ethylhexylacrylate.

Claim 5

Copolymer as defined in claim 1 characterised in that the olefinically unsaturated monomer (C) is selected from (i) methyl methacrylate together with acrylic acid; or (ii) vinyl acetate; or (iii) styrene together with acrylic acid.

Claim 6

Process for the preparation of a copolymer capable of cross linking to provide a thermosetting system, characterised in that monomers of the following three classes are reacted, in the weight percentages given, in solution or in suspension in the presence of a free radical catalyst and at a temperature of from 50° C. to 100° C., (a) from 11% to 30% of an ester mixture consisting of at least 70% by weight of an unsaturated diester of formula (I) r.sub.1 --o.sub.2 c--ch═ch--co.sub.2 --r.sub.2 (i) wherein R 1 represents (a) a monohydroxy alkyl group of two to six carbon atoms; or (b) a group of the empirical formula (II) --(ch.sub.2).sub.n O].sub.m [--(CH.sub.2).sub.x --OH (II) in which formula n=2 or 3; x=2 or 3, and m is from 1 to 800; and R 2 represents a linear or branched primary alkyl group having from 4 to 12 carbon atoms; which ester mixture has been prepared by reacting together 1.0 mole of a polyol of formula R 1 OH, 1.1 moles of a primary alcohol of formula R 2 OH and 1 mole of an acid of formula HO 2 C--CH═CH--CO 2 H, or 1 mole of the anhydride thereof, in the presence of para-toluene sulphonic acid as catalyst; (B) from 2% to 35% of an alkyl acrylate, having up to eight carbon atoms in the alkyl group, which group may be of linear or branched configuration; and (C) from 35% to 87% of at least one other monomer containing olefinic unsaturation, and chosen from the group consisting of methyl methacrylate, acrylic acid, vinyl acetate, and styrene, provided that the percentage amounts of (A), (B) and (C) always total to 100.

Claim 7

Process for the preparation of a copolymer capable of cross linking to provide a thermosetting system, characterised in that monomers of the following three classes are reacted, in the weight percentages given, in solution or in suspension in the presence of a free radical catalyst and at a temperature of from 50° C. to 100° C., (a) from 11% to 30% of an ester mixture consisting of at least 70% by weight of an unsaturated diester of formula (I) r.sub.1 --o.sub.2 c--ch═ch--co.sub.2 --r.sub.2 (i) wherein R 1 represents (a) a monohydroxy alkyl group of two to six carbon atoms; or (b) a group of the empirical formula (II) --(ch.sub.2).sub.n O].sub.m [--(CH.sub.2).sub.x --OH (II) in which formula n=2 or 3; x=2 or 3, and m is from 1 to 800; and R 2 represents a linear or branched primary alkyl group having from 4 to 12 carbon atoms; which ester mixture has been prepared by reacting together 1.0 mole of a polyol of formula R 1 OH, 1.1 moles of a primary alcohol of formula R 2 OH and 1 mole of an acid of formula HO 2 C--CH═CH--CO 2 H, or 1 mole of the anhydride thereof, in the presence of para-toluene sulphonic acid as catalyst; (B) from 2% to 35% of an alkyl acrylate, having up to eight carbon atoms in the alkyl group, which group may be of linear or branched configuration; and (C) from 35% to 87% of at least one other monomer containing olefinic unsaturation, and chosen from the group consisting of methyl methacrylate, acrylic acid, vinyl acetate, and styrene, provided that the percentage amounts of (A), (B) and (C) always total to 100.

Claim 8

Process according to claim 5, characterised in that the reaction is carried out in isopropanol solution under reflux.

Claim 9

Process according to claim 5, characterised in that the reaction is carried out in water in the presence of sufficient surfactant to provide an aqueous emulsion.

Claim 10

Process according to claim 5, characterised in that the reaction is carried out at a temperature of from 65°-75° C.

Claim 11

Process according to claim 5, characterised in that the unsaturated diester used is the reaction product of one of the following combinations of reactants: (i) isobutanol, ethylene glycol, and maleic acid or anhydride; (ii) butanol, ethylene glycol, and maleic acid or anhydride; (iii) 2-ethylhexanol, ethylene glycol, and maleic acid or anhydride; (iv) isobutanol, 1,2-propylene glycol, and maleic acid or anhydride; (v) isobutanol, glycerol, and maleic acid or anhydride; (vi) isobutanol, ethylene glycol, and furmaric acid.

Claim 12

Process according to claim 5, characterised in that the alkyl acrylate is chosen from butylacrylate or 2-ethylhexylacrylate.

Claim 13

Process according to claim 5, characterised in that the olefinically unsaturated monomer (C) is selected from (i) methyl methacrylate together with acrylic acid; or (ii) vinyl acetate; or (iii) styrene together with acrylic acid.

Claim 14

Process according to claim 5, characterised in that the free radical catalyst is chosen from t-butyl peroctoate or ammonium persulphate.