AU726612B2

AU726612B2 - An unsaturated polyester resin composition

Info

Publication number: AU726612B2
Application number: AU73338/98A
Authority: AU
Inventors: Marzio Ligutti; Massimo Montecchi
Original assignee: C O I M SpA CHIMICA ORGANICA
Current assignee: Coim SpA - Chimica Organica Industriale Milanese
Priority date: 1997-04-04
Filing date: 1998-04-01
Publication date: 2000-11-16
Anticipated expiration: 2018-04-01
Also published as: IT1291705B1; ITTO970286A1; EP0971964A1; AU7333898A; WO1998045343A1; CA2296021A1

Description

WO 98/45343 WO985343 PCT/EP98/01 8 8 3 1 An unsaturated polyester resn compositio The present invention relates to an unsaturated olyester resin composition, to its an unsaturated p o l y e s t e r resin compositionals to its use for applications with foamed plastics materials and to articles comprising a core or layer of a foamed plastic material and a layer or coating obtained from said resin composition.

More particularly, the invention relates to a polyester re- sin composition comprising an unsaturated polyester and a monomeric solvent which r poyester and a monomeric solvent which is cross-reactive with said polyes- ter.

Conventional unsaturated polyester resin compositions innclude relatively high amounts of ethylenically unsaturated monomeric Solvents, particularly styrene-based monomeric solvents. The relatively high amount of styrene makes such compositions unsuitabeorToa mon o t y r e n e ma k e s s u c h compositions unsuitable for coating polystyrene foamed plastics materials or generally foamed polymers including styrene as a co-monomer, since the styrene-based solvent attacks and dissolves the polymer containing styrene.

Polystyrene foam is a widely used rigid plastic material; in many cases it is used as an insulation material, in other cases it is used for its structural properties combined with its chemical and water resistance. In many ap- plications, the foam core needs to be covered by a protective layer; reasons therefor might be the need for high impact resistance, fire regulations improving the long term weathering properties and/or asthetic reasons. This is the case, for example, in insulated trailers, insulated containers and buoyancy applications.

There are applications where foamed plastics materials, such as polyurethane, are coated with unsaturated polyester WO 98/45343 WO 985343 PCT/EP98/01883 2 resin or are bonded using unsaturated polyester to a plastics or wood material. In this type of application, there are basically two problems, one relating to the polyurethane and one related to the unsrated polyester resin (ii).turated polyester re- Polyurethane is not always the most appropriate material for many of these applications. In applications, such as refrigerated tIrport n app l i c a t ions, such as refrigerate transport, the insulation is subject to high moisture loads. However, polyurethane is known to be highly moisture sensitive.

In the past, tests have been carried out on insulated truck bodies or trailers which had been in use for several years.

These tests showed that the polyurethane foam cores were soaked with water, hile the extruded polystyrene cores still were practically dry. It is obvious that the insulation value of the wet polyurethane cores was reduced submore.stantially and, thus, did not meet the requirements anymore.

(ii)The unsaturated polyester resins typically employed have a high styrene monomer content (35 to 45% wt); this causes high styrene monomer contents in the manufacturing halls creating an unhealthy working environment. The high styrene monomer contents in the working environment cannot be reduced unless manufacturing process is changed or unless the manufacturing units are restructured including the necessary evacuation units. The use of such evacuation units is not economically feasible in most cases.

There are currently applications where extruded polystyrene foam is used as a core for articles wherein the bonding is carried out by using a polyurethane-based adhesive. How- WO 98/45343 PCT/EP98/01883 3 ever, using a polyester resin as adhesive, instead of polyurethane-based adhesive results in several advantages, one being the fact that polyester resin bonds are less rigid bonds which results in a good mechanical performance to vibrations and dynamic loads. Especially in insulated transport applications this improves the long term performance of the articles.

Another advantage of using polyester resin as adhesive is that polyester adhesives can be employed for reparations, since it provides joint-less repairs. Polyurethane adhesives, however, would not readily enable such joint-less technique.

Furthermore, previous attempts to provide articles includcompositions or bonded articles comprising a layer of polystyrene foam and an unsaturated polyester resin sheet reinforced with glass fibres (GRP) bonded to said layer by means of an unsaturated polyester-based glue were unsuccessful, due to the attack of the polystyrene surface by the relatively high amounts of styrene monomer.

DE-A-12 36 187 describes protecting coatings for foamed polystyrene articles which are obtained by coating the polystyrene foam with a composition containing 25-75 percent by weight wt) of a polymerisable ethylenically unsaturated polyester and 25-75% wt of a polymerisable ethylenically unsaturated monomer of which 50 to 100% wt is an allylether of N-methylol-urea or a derivative thereof.

JP-01319547-A describes moulded articles of polystyrene foam onto which an unsaturated polyester resin is applied; the process comprises coating and/or laminating together WO 98/45343 PCT/EP98/01883 4 with a reinforcing material on a polystyrene foam a resin composition containing 100 parts by weight of unsaturated polyester resin and 5-200 parts by weight of a compound, such as di-cyclo-pentenyl oxy ethyl acrylate or di-cyclopentenyl oxy ethyl meth-acrylate.

JP-63260936-A describes a composite material comprising a ore foam material, such as polystyrene foam and a radical polymerised composition impregnated in the core foam; the composition comprises an unsaturated polyester resin, a cross--linking agent, a curing promoting agent and a curing agent; the cross-linking agent is a monofunctional acryl monomer or a multifunctional acryl monomer.

JP-49021428-A describes a coating composition for thermoplastic mouldings, particularly of polystyrene foam comprising an unsaturated resin and a monoester from (meth) acrylic acid and a C 2

-C

8 polyol or a C 4

-C

18 ether linkagecontaining polyol, or the reaction product of a C 2

-C

1 8 alkylene oxide and (meth) acrylic acid, such as particularly 2 -hydroxyethyl acrylate. Whereas styrene monomer can be used as a co-solvent for the unsaturated polyester together with the above-mentioned compounds, as shown by the working examples, even relatively low amounts of styrene in combination with 2-hydroxy ethyl acrylate caused at least partial erosion of the polystyrene foam.

According to the examples, a partial erosion of the polystyrene foam takes place with the use of a composition comprising about 60% wt of polyester resin and about 32% wt of hydroxy ethyl acrylate (HEA) and as little as about 8% wt of styrene monomer.

It is reported that when HEA is used as the only monomeric solvent, the surface of polystyrene foam does not appear to be substantially eroded; it has been found however that the use of HEA as the only monomeric solvent causes substantial increase of the curing time necessary to achieve the desirable mechanical properties of the polyester coating and a post-curing treatment appears to be required which is undesirable. An increase of the curing time in order to reduce the curing time is not advisable, since higher curing temperatures, such as 70-80 0 C, would be detrimental to foamed plastics materials, in particular polystyrene foams.

The above discussion of documents, acts, materials, devices, articles and the like is included in this specification solely for the purpose of providing a context for the present invention. It is not suggested or represented that any or all of these matters formed part of the prior art base or were common general knowledge in the field relevant to the present invention as it existed in Australia before the priority date of each claim of this application.

Throughout the description and claims of the specification the word "comprise" and variations of the word, such as "comprising" and "comprises", is not intended to exclude other additives, components, integers or steps.

Therefore, it would be highly desirable to provide an improved polyester resin composition which contains lower amounts of monomeric styrene without impairing the mechanical properties thereof and which does not dissolve 20o polystyrene foam or styrene-based copolymer foams. It would also be desirable S• to have coated and/or bonded articles including a foam core or layer, wherein the o foam does not undergo surface degradation or chemical attack when in contact with a polyester resin.

It would be desirable to provide an improved polyester resin composition S. 25 which does not dissolve polystyrene foam or styrene-based copolymer foams or in general polymers obtained from the polymerisation of ethylenically unsaturated monomers.

It would also be desirable to provide a polyester resin composition having a reduced amount of styrene monomer, without impairing the mechanical properties of the cured polyester resin.

It would even further be desirable to provide coated and/or bonded articles including a core or layer of a styrene polymer or copolymer foam or in general polymers obtained from the polymerisation of ethylenically unsaturated monomers and a coating of an unsaturated polyester resin, wherein the foam does not -6undergo surface degradation or chemical attach and/or delamination as a result of a contact with the polyester resin.

It would even further still be desirable to provide a process for coating foams of styrene polymers or copolymers or in general polymers obtained from the polymerisation of ethylenically unsaturated monomers with a layer of polyester resin having structural properties or for bonding sheets, such as GRP sheet or plywood sheets, to said polymers by means of a polyester-based adhesive.

It would yet even further be desirable to provide a polyester resin composition which allows application on foamed materials without causing unacceptable styrene-monomer emissions in the working environment.

Being able to use polystyrene-based foam for making articles by bonding sheets, by way of an unsaturated polyester resin composition results in better workability as there is no dust creation during cutting operations of polystyrenebased foams. Further, polystyrene foam is mechanically recyclable, while polyurethane is not; this improves the end product and the manufacturing process from the environmental point of view.

Secondly, the present invention offers even more opportunities to improve the properties of the manufactured articles, because the mechanical properties of extruded polystyrene are superior than those of polyurethane of equal density.

2o This means that articles that have a constructive aspect/role have either an improved performance, or can be optimised.

Another aspect of the present invention is that extruded polystyrene foam o hardly takes up any water, is to a very high degree resistant to moisture and has a very high resistance to a broad range of chemicals. This results in a superior long term performance of the articles made thereof a refrigerated truck body, an insulated container, a pontoon).

According to the invention, it has been found that some of these are achieved when the polyester resin composition comprises, as the monomeric solvent, styrene and an hydroxy alkyl acrylate or methacrylate in a defined ratio SC 30 with respect to the amount of unsaturated polyester.

In one aspect the present invention provides an unsaturated polyester resin composition comprising an unsaturated polyester and a monomeric solvent reactive with said polyester, wherein said unsaturated polyester is in the amount \R of from 65 to 80% wt and said monomeric solvent is in the amount of from 35 to wt referred to the total amount of unsaturated polyester and solvent, the monomeric solvent comprises styrene and hydroxyalkyl-acrylate or -methacrylate, wherein alkyl is C, to C4 and wherein the amounts of styrene, hydroxy alkyl (meth)acrylate and unsaturated polyester in said composition comply with the following equation in parts by weight:

(I)

Styrene (parts wt) Polyester (parts wt) hydroxy alkyl (meth) acrylate (parts wt) 1218 It has been found that values of the above mentioned ratio lower than 0.12 do not provide a suitable chemical bonding of the polyester onto the styrene polymer or copolymer foam a a a **e WO 98/45343 PCT/EP98/01883 8 whereas values higher than 0.18 cause an at least partial surface degradation and/or dissolution of the foam; preferred values for the above ratio are between 0.16 to 0.18.

The teaching of the invention allows to provide polyester resin compositions including an amount of polyester varying in a wide range, preferably from 65% wt to 80% wt and more preferably between 65% and 75% wt, referred to the total amount of unsaturated polyester and monomeric solvent. Correspondingly, the amount of monomeric solvent in the composition is preferably from 35 to 20% wt and more preferably from 35 to 25% wt. The amount of styrene monomer in the monomeric solvent is preferably from 10 to 16% wt referred to the amount of polyester and monomeric solvent. According to the teaching of the invention, if the amount of styrene in said polyester resin composition is increased, for example by 1% wt, correspondingly, the amount of hydroxy alkyl (meth)-acrylate is to be increased in the amount of 5.55% wt to 8.33% wt, in order to provide a polyester resin composition which does not detrimentally affect the surface of the styrene polymer or copolymer foam or in general polymers obtained from the polymerisation of ethylenically unsaturated monomers.

The unsaturated polyester in the composition is preferably the product of esterification of a glycol, an unsaturated dicarboxylic acid or anhydride and optionally a saturated dicarboxylic acid or anhydride; preferably, in the presence of a chain termination agent which is preferably an allyl ether of a C 3

-C

10 polyol, most preferably a diallyl ether of C 3

-C

10 aliphatic or cycloaliphatic polyol, such as glycerol, trimethylol propane or ethane.

Suitable glycols comprise ethylene glycol, diethylene glycol, tri-ethylene glycol, polyethylene glycol, propylene WO 98/45343 PCT/EP98/01883 9 glycol, di-propylene glycol, tri-propylene glycol, polypropylene glycol, 2,2-di-methylpropane diol, 1, 3 -butane diol, 1, 2 -butylene glycol, 2 ,3-butylene glycol.

The unsaturated acid or anhydride is preferably maleic or fumaric acid or anhydride; however, also itaconic acid and chloromaleic acid or anhydride may conveniently be used.

Mixtures of different unsaturated acid or anhydrides may also be used.

The saturated acid or anhydride, when used, is preferably selected from the group consisting of phthalic acid, tetrahydrophthalic acid, cyclohexane dicarboxylic acid, adipic acid, sebacic acid, succinic acid, azelaic acid, isophthalic acid, terephthalic acid and the corresponding anhydrides, HET acid and chlorendic anhydride and mixtures thereof.

Usually, a slight molar excess of glycol is used with respect to the overall amount of the acid, such as preferably a 5 to 20% molar excess.

The chain termination agent, is preferably trimethylol propane diallyl ether.

The unsaturated polyester of the present invention typically has an acid unsaturation index, expressed as the ratio between the number of equivalents of unsaturated acid in the polyester and the total number of equivalents of acid in said polyester, higher than 0.50, more preferably not lower than 0.70, and most preferably not lower than 0.85.

The average numerical molecular weight (Mn) of the polyester is preferably from 800 to 1400; and the average weight molecular weight (Mw) is preferably from 1800 to 2300.

WO 98/45343 PCT/EP98/01883 The polyester resin composition has preferably an overall percentage of unsaturations, expressed as the ratio between the total number of unsaturated moles in the composition (polymer plus solvent) and the total number of moles from which the polyester resin composition is obtained, from 0.55 to 0.75.

The polyester resin composition has preferably an acid number of from 30 to 50 mg KOH/ml, an hydroxyl number of from to 105 mg KOH/ml.

The polyester resin composition of the present invention may further comprise additives which are usually present in conventional unsaturated polyester resin compositions such as inhibitors, storage stabilisers, curing promoters and inorganic fillers. Preferred inhibitors are hydroquinone and toluene hydroquinone. Preferred promoters are the socalled metal soaps, such as cobalt, copper or vanadium octoate, naphthenate and acetonate.

such as particularly methyl-ethyl-ketone (MEK) peroxide and methyl isobutyl ketone peroxide. A typical curing system consists of 0.2% wt cobalt octoate wt Co), 2% wt of a MEK-MEK peroxide solution (50% by weight for each component in the solution), referred to 100 grams polyester resin composition. The resin composition has preferably a curing time of from 8 to 15 minutes, a gel time of from 10 to minutes and an exothermic peak of about 150-170 0

C.

The preferred use of the resin composition of the present invention is for coating the surface of foamed articles.

WO 98/45343 PCT/EP98/0188 3 11 The foamed materials on which the resin composition can be applied include polystyrene foam (extruded and expanded), syndiotactic polystre e a n d e x p a n d e d Asyndiotact olystryrene, styrene copolymer foams, such as ABS, polyurethane foam, polyethylene terephtalate

(PET)

foam, polypropylene foam, polyethylene foam, polyphenyl ether foam and polyvinyl chloride (PVC) foam. The application is carried out by means of conventional methods, such as brushing, rolling, spraying or dipping and other existing known methods. The coating layer may have a thickness higher than I mm and preferably in the range of from 2 to mm. After application the coating layer is cured according to conventional methods. The curing temperature is typically with the range of from 15 0 C (ambient temperature) to 0

C.

Additionally, the polyester resin composition according to the invention may be used as an adhesive in order to bond sheets of conventional unsaturated polyester resin to the surface of said foamed articles. The temperature of the press plates, within which the resin composition is cured, may range between 30 0 C and 60 0 C. The preferred temperature of the press plates is between 30 0 C and 40 0

C.

Furthermore, the polyester resin composition of the present invention can be used as a primer coating of foamed articles which can then be either coated or bonded with any conventional unsaturated polyester resin. Accordingly, the invention comprises within its scope articles comprising a core or layer made of a foamed material and at least one layer (either as a coating or as an adhesive) obtained from the polyester resin composition of the present invention.

Also comprised within the scope of the invention are articles as above defined having an additional primer coating layer cosisting of the polyester resin composition of the WO 98/45343 PCT/EP98/0188 3 12 present invention which is applied between the surface of said foamed core and any conventional unsaturated Polyester resin (either used as a coating or an adhesive).

The resin composition may also be used to manufacture composite materials, wherein the Polyester resin composition according to the invention is reinforced by fabric, mats and/or fibres.

Preferred applications of the polyester resin composition of the present invention are for manufacturing sandwich panels having a core of polystyrene foam, such as panels for thermally insulated trailers or containers. The polyester resin composition of the present invention is also suitable to manufacture coated parts for marine applications, such as pontoons.

Exaple 1 PREPARATION OF POLYESTER RESIN

COMPOSITION

12.55 parts by weight of propylene glycol, 24.25 parts by weight dipropylene glycol, 7.04 parts by weight phthalic anhydride 8.9 parts by weight trimethylol propane diallyl ether, 31.99 parts by weight fumaric acid, 0.01 parts by weight hydroquinone are charged into a reactor equipped with a mixer, a partial condenser and a shielding gas sys- tem. The esterification reaction is carried out under nitrogen gas flow by the conventional fusion method at a temperature of from 175 to 180 0 C by periodically checking the viscosity into the reactor, until the acid value of the polyester resin has value from 36 to 47 mg KOH/ml. The reaction product was then cooled to 150 0 C and discharged into a dilutor vessel containing 15 parts by weight styrene and 12 parts by weight hydroxy-ethyl-methacrylate and 0.002 part by weight copper naftenate while taking care that the internal temperature in the dilutor vessel is not higher WO 98/45343 PCTIEP98/01883 13 than 80 0

C.

The obtained polyester resin composition has a polyester polymer content of about 74% wt. The polyester has an acid unsaturation index of Tests were carried out in order to confirm that the polyester resin composition of the present invention could be applied onto a polystyrene foam and to check the compatibility, chemical attack (Example 2) and the tensile bond strength (Example 3) of polystyrene sandwich panels.

In all the tests, the polyester resin composition was cured with a curing system consisting of 0.2% wt of cobalt octoate wt Co) and 2% wt of a MEK-MEK peroxide solution by weight for each component in the solution), referred to 100 grams polyester resin.

Example 2

COMPATIBILITY

In a first series of laboratory tests, the compatibility of the polyester resin of this invention with the polystyrene foam was evaluated as follows: a first set of samples (Combination 2A) was prepared, wherein the polyester resin composition of Example i, to which the curing system has been added, was poured on top of a STYROFOAM* RTM polystyrene board (Trademark of The Dow Chemical Company) and distributed uniformly by means of a brush, in order to obtain a layer having a thickness of 2-4 mm. After curing of the polyester resin at ambient temperature(about 250C), a hardened layer of polyester bonded to the polystyrene surface was obtained.

According to the same procedure, another two sets of samples were made, one combining the STYROFOAM* RTM polystyrene WO 98/45343 PCT/EP98/01883 14 with the commercially available polyester resins

(EXTER

102S available from CM S p yest e r r e s i n s E X

T

E R 102S available from COIM (Combination 2B) and one combining the polyester resin of the invention (Example 1) with polyurethane having a density of 40 kg/ 3 (Combination 2C). Visual comparison between the 3 combinations showed that on the set of samples of the Combinations 2A and 2C there was no chemical attack or dissolution and the surface coating was smooth.

In addition, the coating layer was removed from the foam of each of the above-described three combinations. Visual inspection and comparison showed again that the surface had not been chemically attacked in the Combinations 2A and 2C, and had not degraded, which was the case in the Combination 2B.

Xple 3 BONDING

PROPERTIES

Another series of tests was carried out in order to measure the bonding properties and to prove the technical feasibility of the coating process. These tests were carried out by bonding a 2 mm GRP sheet (manufactured by General Plast, Italy) to a foam core by using the unsaturated polyester resin of the present invention. Approximately i kg of resin was used per square meter resulting in a 1 mm thick coating layer.

The tensile bonding strength and the tensile modulus were measured according to ASTM D-1623. The shear bonding strength and the shear modulus were measured according to ASTM C-273.

A set of samples was prepared for each foam type, i.e. polystyrene foam and polyurethane foam. The polystyrene foam used was an extruded polystyrene foam STYROFOAM*

RTM,

(*trademark of The Dow Chemical Company), having a density WO 98/45343 PCT/EP98/01883 of 40 kg/m 3 (set 3A) and was coated with the unsaturated Polyester resin of Example 1. For comparison purposes, a polyurethane foam was coated o r compariso n p u r p o s e s a polyurethane foam was coated with a commercially available unsaturated polyester resin (EXTER 102S from COIM S.p.A.) (set 3B). The polyurethane used was a 40 kg/m 3 density rigid polyurethane foam commercially available.

In all samples, the foam cores were 50 mm thick. Curing was done under a pressure of 0.5 kg/cm 2 and at 50 0

C.

Average tensile bonding strength values measured on samples according to the present invention (set 3A) were: 424 kPa; and the shear bonding strength tests gave shear bonding strengths of 354 kPa.

The measurements on the polyurethane foam samples (set 3B) gave: tensile bonding strength of 337 kPa and the shear strength of 210 kPa.

Exampe 4 BONDING VS. COATING Further mechanical tests were carried out to confirm the above tests and to compare the bonding technique to the coating technique.

For this purpose, one set of samples comprising extruded polystyrene foam STYROFOAM* RTM were bonded to a 2 mm GRP sheet (commercially available from General Plast, Italy) using the polyester resin of the invention (set 4A) and another set of samples comprising said polystyrene foam were coated with a 3 mm thick layer of the polyester resin of the present invention (set 4B). The bonded samples were cured under pressure (0.5 kg/cm 2 and at 50 0 C. The coated samples were cured at room temperature under pressure kg/cm 2 WO 98/45343 PCT/EP98/018 83 16 For the bonded samples (set 4A), the average tensile bonding strength was of 650 kPa, and the average shear strength was of 493 kPa and the erag s h e a r s t r e n g t h was of 493 kPa and the average shear modulus was of 5,836 kPa.

For the coated samples (set 4B), the average tensile bonding strength 600 kPa, the average shear strength 513 kPa and average shear modulus 6,219 kPa.

The tests also show that the invention applied on extruded polystyrene foam having a density of 40 kg/m 3 provides results typically 30 to 50 percent better than the results obtained by the existing techniques applied on polyurethane rigid foam also having a density of 40 kg/m 3

Claims

1. An unsaturated polyester resin composition comprising an unsaturated polyester and a monomeric solvent reactive with said polyester, wherein said unsaturated polyester is in the amount of from 65 to 80% wt and said monomeric solvent is in the amount of from 35 to 20% wt referred to the total amount of unsaturated polyester and solvent, the monomeric solvent comprises styrene and hydroxyalkyl-acrylate or -methacrylate, wherein alkyl is C 1 to C4 and wherein the amounts of styrene, hydroxy alkyl (meth)acrylate and unsaturated polyester in 0o said composition comply with the following equation in parts by weight: (I) Styrene (parts wt) 0. 12-0.18. Polyester (parts wt) hydroxy alkyl (meth) acrylate (parts wt)

2. A composition according to claim 1, wherein the unsaturated polyester is the product of esterification of a glycol, at least an unsaturated dicarboxylic acid or anhydride, optionally a saturated dicarboxylic acid or anhydride and a chain termination agent consisting of an allyl ether of a C 3 -C 10 polyol.

3. A composition according to claim 2, wherein said unsaturated dicarboxylic j 20 acid or anhydride is selected from the group consisting of maleic acid or anhydride, fumaric acid or anhydride, itaconic acid and chloromaleic acid or anhydride and mixtures thereof.

4. A composition according to claim 2, wherein said unsaturated acid or V 25 anhydride is selected from the group consisting of phthalic acid or anhydride, tetra-hydrophthalic acid or anhydride, cyclohexane dicarboxylic acid or anhydride, adipic acid, sebacic acid, succinic acid, azelaic acid, isophthalic acid, terephthalic acid or anhydrides, HET acid, chlorendic anhydride and mixtures thereof.

5. A composition according to claim 2, wherein said chain termination agent is trimethylol propane diallyl ether. -18-

6. A composition according to claim 1, wherein said glycol is selected from the group consisting of ethylene glycol, diethylene glycol, tri-ethylene glycol, polyethylene glycol, propylene glycol, di-propylene glycol, tri-propylene glycol, polypropylene glycol, 2,2-di-methylpropane diol, 1,3-butane diol, 1,2-butylene 2,3-butylene glycol and mixtures thereof.

7. A composition according to any one of claims 1 to 6, wherein the unsaturated polyester has an acid unsaturation index, expressed as the ratio between the number of equivalents of unsaturated acid in the polyester and the i0 total number of equivalents of acid in said polyester higher than 0.50.

8. A composition according to any one of claims 1 to 7, wherein the unsaturated polyester has an acid unsaturation index not lower than 0.70.

9. A composition according to any one of claims 1 to 8, wherein the polyester has an acid unsaturation index not lower than 0.85. A composition according to any one of claims 1 to 9, wherein the polyester :resin composition has an overall percentage of unsaturations, expressed as the o° 20 ratio between the total number of unsaturated moles in the composition (polymer :.,,oplus solvent) and the total number of moles from which the resin composition is obtained, from 0.55 to 0.75.

11. A composition according to any one of the preceding claims, wherein the oo°.t 25 resin composition has an acid number of from 30 to 50 mg KOH/ml, and a hydroxyl number of from 50 to 105 mg KOH/ml, and a hydroxyl number of from to 105 mg KOH/ml. A composition according to any one of the preceding claims, comprising 30 from 65% to 75% wt of unsaturated polyester and from 35 to 25% wt of monomeric solvent.

13. A composition according to any one of the preceding claims, comprising f- ,from 10 to 16% wt styrene referred to the overall composition. \V\P Il\SJ-mc\73 ]33X.,} -19-

14. A composition according to any one of the preceding claims, comprising inhibitors selected from hydroquinone and toluene hydroquinone.

15. A composition according to any one of the preceding claims, further comprising curing promoters and/or fillers.

16. An unsaturated polyester resin composition according to the preceding claims, wherein the ratio according to equation is of from 0.16 to 0.18.

17. A polyester resin composition according to claim 1 substantially as hereinbefore described with reference to any of the examples. DATED: 1 June, 2000 PHILLIPS ORMONDE FITZPATRICK Attorneys for: C.O.I.M. S.p.A. CHIMICA ORGANICA 20 INDUSTRIALE MILANESE W:\onl;l\Species\73338.ldoc