HYDROCARBON RESINS

Abstract: Hydrocarbon resins compatible with wax and ethylene-­ vinyl acetate copolymers and with a satisfactory softening point useful in hot melt adhesives are prepared by polymerising in the presence of a Friedel-Crafts catalyst-5 to 30 parts by weight of vinyl toluene, 15 to 45 parts by weight of styrene and 40 to 70 parts by weight of alpha-methyl styrene.

Description: Hydrocarbon Resins This invention relates to hydrocarbon resins and their production. In particular the invention relates to resins compatible with wax and ethylene-vinyl acetate copolymers and with satisfactoryDs±)ftening point. Canadian Patent 946 543 concerns the production of terpolymers by the polymerisation of 10 to 80 wt % of vinyl toluene, 10 to 80 wt % e.g. 10-50 wt.% of alpha-methyl styrene and 10 to 50 wt.t of styrene, the mole ratio of vinyl toluene to styrene being from 3:1 to 1:1. Such resins however have been found to have relatively high cloud points (about 175"C) and this makes them unsuitable for use as a blend with wax ethylene-vinyl acetate copolymers as coating compositions where clouding would readily occur. United Kingdom Patent 1451524 concerns a copolymer of alpha-methyl styrene and styrene wherein the proportion by weight of the former ranges from 50 to 90% and which has a softening point (ring and ball) of from 70*C to 1000C. In accordance with this invention polymers are prepared in high yield of low colour to water-white by polymerising in the presence of a Friedel-Crafts catalyst 5 to 30 parts by weight of vinyl toluene, 15 to 45 parts by weight of styrene and 40 to 70 parts by weight of alpha-methyl styrene. Resins prepared by this process comprise polymers of 5 to 30 parts by weight of units derived from vinyl toluene, 15 to 45 parts by weight of units derived from styrene and 40 to 70 parts by weight of units derived from alpha-methyl styrene. Compared with the resins disclosed in UK Patent 1451524 the replacement of part of the styrene by vinyl toluene leads to improved compatibility with wax and ethylene-vinyl acetate copolymers without a significant effect on the resin softening point. Although the polymerisation feed has to have 40 to 70 wt % of alpha-methyl styrene, it is preferred that 50 to 60% by weight of alpha-methyl styrene be used. The preferred amounts of styrene and vinyl toluene are 20 to 40 wt % of styrene and 10-25 wt % of vinyl toluene. The individual vinyl toluene isomers may be used as well as mixtures of two or more of them. The three monomers are preferably dissolved in a solvent, for example aromatic, aliphatic or mixed solvents. Specific examples 9f solvents are alkanes, for instance, n-heptane, n-octane; benzene, toluene and alkylated benzenes, for instance the mixed alkyl substituted benzenes known as Solvesso 100. Generally the monomers are dissolved in 50 to 250 parts, for example about 100 parts, by weight of solvent for hundred parts by weight of total monomer. Suitable Friedel-Crafts catalysts include aluminium chloride, aluminium bromide, aluminium chloride/hydrochloric acid/aromatic hydrocarbon complex or aluminium chloride/alkyl halide/aromatic hydrocarbon complex. In the former complex the aromatic hydrocarbon is preferably an alkylated hydrocarbon, e.g. o-xylene, mesitylene, ethyl benzene or isopropyl benzene and in the latter complex the alkyl chain of the alkyl halide can be linear or branched and can vary from 1 to 30 carbon atoms. Other suitable Friedel-Crafts catalysts are acid liquid AlCl3 sludges obtained as by-products during the alkylation of benzene or any other substttuted aromatics (e.g. toluene or xylenes) with branched chain olefins. Apart from aluminium trichloride, the preferred Friedel-Crafts catalyst is boron fluoride gas or a complex phenol, ether or acetic acid. Other BF3 complexes can be used. Generally, from 0.1 to 5 wt %, e.g. 0.2 to 1.5 wt % of Friedel-Crafts catalyst based on the total weight of monomers is used. Generally it is preferred that the reaction temperature be kept below 50-C, preferably below 45 C. Resin yields of over 60% are usually achieved and these yields may often be between 70 and 80t and sometimes higher. After polymerization the residual catalyst is removed by for example washing with aqueous solution of alkali, ammonia or sodium carbonate. The final resin is stripped of unreacted hydrocarbons and low molecular weight oil oligomers for example by steam stripping or vacuum distillation. The finished resin has a softening point of from 40eC to 160 C preferably 60 C to 160-C, usually 80" to 110 C. The Gardner colour is usually less than 1. For optimum use in hot melt adhesive formulations the resins should preferably have a softening point in the range 750C to 115 C preferably 90 C-105 C. The resins obtained can be used in many applications which require low viscosity, good flexibility and elongation before or especiallyafter chemical modification with polar compounds such as phenols, unsaturated anhydrides such as maleic anhydride or unsaturated acids (e.g. fumaric acid). These resins are designed for a wide range of end uses and applications. They can be applied to paper, metal, thermo-plastic films, Cellophane (Registered Trade Mark), polyester, PVC, woven or non woven fabrics, glass etc. and for bonding such materials together. Typical applications are hot melts, carpet backing, coatings, e.g. coating with drying oil formulations, book binding, paper sizing or in any applications involving natural or synthetic and/or rubbers such as caulks, sealants or rubber tackification. The main applications involving such resin properties are pressure sensitive adhesives, hot melt adhesives, hot melt pressure sensitive adhesives, low temperature adhesives, label adhesives, latex adhesives, surgical tapes and masking tapes where they may be blended with polymers such as ethylene/vinyl acetate copolymers and optionally with wax. Also they may be used as tackifiers with natural rubber or synthetic rubbers such as polyisoproprene, EPDM, butyl, chlorobutyl, bromobutyl, neoprene and block copolymers for example styrene/butadiene and styrene/isoprene rubber (i.e. Shell Cariflex (Registered Trade Mark) TR1107) and mixtures of such rubbers. The resins may also be emulsified in water and the emulsions used as tackifiers for water based adhesives such as those based on polyacrylates and carboxylated styrene butadiene copolymers. The resins may conveniently be emulsified by the techniaues described in our European Patent Application According to this invention one can use as a component in an adhesive formulation a resin which is a copolymer containing from 40 wt % to 70 wt % of units derived from alpha methyl styrene, from 5 wt % to 30 wt % of units derived from vinyl toluene and from 15 wt % to 45 wt % of units derived from styrene. In particular the present invention provides a hot melt adhesive comprisina (i) an ethylene vinyl acetate copolymer, preferably 20 to 30 wt % (ii) wax, preferably 40 to 60 wt * and (iii) a resin which is a copolymer containing from 40 wt % to 70 wt % of units derived from alpha methyl styrene, from 5 wt % to 30 wt % of units derived from vinyl toluene and from 15 wt 8 to 45 wt % of units derived from styrene. EXAMPLE 1 A two-litre flask was equipped with stirrer, thermometer, reflux condenser, nitrogen inlet, addition funnel containing 200 q alpha-methyl styrene, 100 g vinyl toluene, 100 q styrene and 400 g n-heptane, and a graduated tube containing 4.8 g AlCl3 powder. The monomers were freshly distilled and the monomers and solvent were dried over molecular sieves. One tenth of the monomer/solvent charge was added to the reactor together with one tenth of the AlCl3 charge and stirred vigorously for 10 minutes, while keeping a constant temperature of 23 + 2-C. The remaininq monomer/solvent and catalyst were added in the same manner in nine successive portions. After total monomer addition, the reaction mixture was stirred for additional 30 minutes at 20-25"C. At this stage, 100 gram water were introduced in the reactor to hydrolyse remaininq catalyst and the aqueous phase was separated. The polymer was then washed with 100 gram of 15 z aqueous ammonia solution. After separation of the aqueous phase, the polymer was distilled under nitrogen up to a pot temperature of 2500C to remove the solvent and eventual unreacted monomers and then steam sparged to 2400C until the water to oil ratio in the condenser receiver was 20:1. In this way, 350 q of a crystal clear white resin was obtained (87.5 % yield based on the monomers). The resin had a rinq and ball softening point of 110 C and a cloud point of 140 C (cloud point of a blend consisting of 25 % wt resin, 25 % ethylene-vinyl acetate copolymer of melt index = 25, and vinyl acetate contentof 28% and 50 % wt paraffin wax of melting point = 68 C). The results obtained above are shown in Example dl in the following Table 1 which also indicates the results obtained by the process of this invention (Examples d2, 3, f1, gi and hi.) for different monomer ratios and different reaction conditions. Examples al, 2 and 3, b1, cl and el are included to show the results obtained when carrying out prior art processes. In comparing e.l with d.1. it is seen that the resin of our invention has a considerably lower cloud point. In comparing our resins with alpha-methyl styrene-styrene resins (a1, 2, 3, b-l) our terpolymers have a lower cloud point at comparable softening points and are thus more compatible in wax, ethylene-vinyl acetate blends. Table 1 MONOMERS EXAMPLE NO TEMP.( C) RESIN YIELD FILL YIELD SOFT. PT. WAX CLOUD PT. GARDNER COLOUR (Part wt.) (%) (%) ( C) ( C) (&alpha;MS:50 a.1 23 88.4 8 105 140 < 1 ( ST:50 a.2 33 89.1 10.1 92 102 < 1 a.3 43 85.5 12.5 82 90 < 1 (&alpha;MS:60 b.1 23 87.1 8.5 97 101 < 1 ( ST:40 (&alpha;MS:70 c.1 23 73 18.5 73 < 70 < 1 ( ST:30 (&alpha;MS:50 d.1 23 87.5 6.8 110 140 < 1 ( ST:25 ( VT:25 d.2 33 86.6 8.8 100 104 < 1 d.3 43 80 16 84 < 70 < 1 (&alpha;MS:25 e.1 23 92.6 4.9 110 175 < 1 ( ST:25 ( VT:50 (&alpha;MS:60 f.1 23 83.6 13.3 104 113 < 1 ( ST:20 ( VT:20 (&alpha;MS:70 g.1 23 76.4 17.4 95 86 < 1 ( ST:15 ( VT:15 (&alpha;MS:50 h.1 43 90 10 93.5 93 < 1 ( ST:40 ( VT:10 Polymerisation conditions: 100 pt. wt. monomer; 100 pt. wt. n-heptane; 1.2 pt.wt. AlCl3 Example 2 Three terpolymers (Resins A,B and C) were prepared derived from 50 parts by weight of d -methyl styrene, 25 parts by weiqht of vinyl toluene (60/40 mixture of meta and para isomers) and 25 parts by weight of styrene. All these resins were prepared by polymerising under a nitroqen blanket the three monomers dissolved in a solvent, 100 parts by weight of Solvesso 100 for Resin A and 100 parts by weight of n-heptane for Resins B and C. 1.2 parts by weight of AlCl3 were used as the catalyst. After polymerisation the reaction mixture was first hydrolysed with water and Corexit (a demulsifier), followed by neutralisation with NH40H. After neutralisation the solvent and unreacted monomers were distilled under a nitrogen stream up to a pot temperature of 250"C and then steam sparged at 2500C until the ratio of water to oil collected in the receiver was about 20:1. The resins was stabilised by the addition of 0.2 wt.% of Irqanox, an antioxidant. In order to test the hot melt adhesive properties of resins A and B and compare them with two other commercial resins (Kristalex and Escorez 5000 a hydrogenated, thermally polymerised polycyclopentadiene) resin blends of the followinq compositions were prepared: Resin 45 pt. by wt. Escorene UL02528 (ethylene Vinyl acetate copolymer ) 45 pt. by wt MF1(1)=25; vinyl acetate 28%) ML 445 wax (a hydrocarbon wax) 10 pt. by wt Irganox 1076 (an antioxidant) 0.5 pt. by wt and resins prepared by processes generally described in United States Patent 3000868 and German Patent 2406618. (1) Melt Index ASTM D1238-79 Table 2 gives some properties of the resins together with adhesive properties of the resin blends. It can be seen that usually at similar softening points Resins A,B and C have higher compatibility than other resins. Table 2 Adhesive Properties Formulation: Resin: 45 pt.wt.; Escorene UL 02528: 45 pt.wt.; ML 445 wax: 10 pt.wt.; Irganox 1076: 0.5 pt. wt. TYPE Made According to Made according Kristallex Escorez Resin A Resin B Resin C U.S.P.3000868 to German Patent F100 5000 2406618 Composition: methyl styrene 25 25 70 45 50 50 50 (% wt.) vinyl toluene 75 75 - - Kr.F100 E-5300 25 25 25 styrene - - 30 55 25 25 25 Softening Point ( C) 88 105 77 100 98 100 76 84 104 Wax Cloud Point ( C) 108 108 < 70 150 115 < 80 < 70 < 70 132 Blend Cloud Point ( C) > 250 115 88 > 250 180 112 85 97 > 250 Viscosity 180 C (Pa.S) 19 32 18.5 20.5 23.5 16.5 15.5 16 21.5 Viscosity 180 C (Pa.S) 20 32 18 20 23.5 21.5 16.5 17 22.5 (after 150H/180 C) 1500 Polyethylene T-peel (g/cm)(1) 330 250 590 330 350 1200 500 500 350 Aluminium T-peel (g/cm) (1) 1100 500 1250 850 740 2.3 1300 1100 925 Yield Point (MPa) 2.5 2.9 1.8 2.9 2 4.9 1.7 2.1 2.6 Tensile Strength (MPa) 4.9 4.7 5.4 5.4 6.1 730 65 4.7 6.2 Elongation (%) 690 650 920 610 670 -22 950 760 700 Brittleness Temp. ( C) -23 -26 -20 -26 -23 - -19 -17 -20 Catalyst BF3 BF3 BF3.Ph. AlCl3 AlCl3 AlCl3 AlCl3 (1) T-Peel Test PSTC-1

Claims: Claims 1 A process for preparing a resin which comprises polymerising in the presence of a Friedel+Crafts catalyst 5 to 30 parts by weight of vinyl toluene, 15 to 45 parts by weight of styrene and 40 to 70 parts by weight of alpha-methyl styrene. 2 A process according to claim 1 wherein the amount of vinyl toluene is 10 to 25 parts by weight, the amount of alpha-methyl styrene is 50 to 60 parts by weight and the amount of styrene is 20 to 40 parts by weight. 3 A process according to either of claims 1 and 2 wherein the monomers are dissolved in 50 to 250 parts by weight of solvent per hundred parts by weight of total monomers. 4 A process according to any one of the preceding claims wherein the catalyst is aluminium trichloride. 5 A resin whenever prepared by the process according to any one of the preceding claims. 6 A hydrocarbon resin comprising 40 to 70 wt % of units derived from alpha methyl styrene, 5 to 30 wt % of units derived from vinyl toluene and 15 to 45 wt % of units derived from styrene. 7. A hydrocarbon resin according to Claim 6 containinq 50 to 60 wt.% of units derived from alpha methyl styrene. 8 A hot melt adhesive comprising (i) an ethylene-vinyl acetate copolymer, (ii) wax; and (iii) a resin according to any one of claims 5, 6 and 7. 9 The use of the resin according to any of claims 5 6 or 7 in hot melt pressure-sensitive adhesive, in a hot melt adhesive or in a coating.

Inventors: WOUTERS, GUY
Applicants: EXXON CHEMICAL PATENTS INC.
Application year: 1986
Main classification: C08F212
IPC codes: C09J191, C08L101, C08L25, C08L23, C08L21, C08L7, C09J123, C09J127, C08F212, C08L33