LOW STYRENE EMISSION VINYL ESTER RESIN EMPLOYING DRYING OILS FOR FIBER-REINFORCED APPLICATIONS

Abstract: The present invention is a low styrene emission, VER composition containing: (1) a VER which is an esterification product of a polyepoxide and a monounsaturated monocarboxylic acid; (2) styrene as a reactive diluent; (3) paraffin as a styrene emission inhibitor; and (4) a drying oil as an adhesion promoter for fiber-reinforced application. The drying oil is present in an amount sufficient to increase the adhesion characteristics of the VER composition with a reinforcing material used therewith. The composition of this invention is useful in fabricating a range of fiber-reinforced plastic structures and equipment.

Description: This invention relates to an improved novel low styrene emission vinyl ester resin formulation which exhibits desirable adhesion characteristics in fiber-reinforced applications. Vinyl ester resins (hereinafter VER) are useful in corrosion resistant applications such as pipes, vessels, scrubbers and smoke stacks. Also, VER are utilized in the fabrication of glass fiber-reinforced products. The VER are admixed with styrene as a reactive diluent to reduce the viscosity of the VER. The presence of styrene in the VER composition results in the emission of styrene vapors into the work atmosphere. Due to the increased attention given to styrene from the industrial hygiene point of view, several methods of reducing the styrene emission have been described in the art. One such method, described in Nylander, US-A-4,201,826, includes the addition to the unsaturated polyester/styrene composition of a film-forming additive such as paraffin wax to inhibit the vaporization of the styrene. Although the paraffin wax provides a desirable decrease in styrene vapor emission, it has been found that the paraffin wax additive results in a substantial loss in the adhesive' properties of the VER to the reinforcing medium. From DD-A-24l 336 unsaturated polyester resin compositions are known which comprise styrene as a reactive diluent, paraffin wax as styrene emission inhibitor and an organic silane compound and/or monoglycerides as adhesion promotor. There is stated that the low styrene emission polyester resin compositions known up to the teaching of said reference have the disadvantage that the adhesion promotor may be separated at low temperatures resulting in loss of effect. From US-A-4, 559, 375 a low styrene emission VER composition is known which contains (1) a VER which is an esterification product of polyepoxide and a monounsaturated monocarboxylic acid, (2) styrene as a reactive diluent, (3) paraffin as a styrene emission inhibitor and Lanolin as an adhesion promotor present in an amount sufficient to increase the adhesion characteristics of the VER composition with the reinforcing material used therewith. It is the object of this invention to provide a further adhesion promotor for low styrene emission VER compositions which exhibits adhesion properties comparable to or improved over a VER composition without the paraffin wax additive. This object is attained by a low styrene emission, VER composition containing (1) a VER which is an esterification product of a polyepoxide and a monounsaturated monocarboxylic acid, (2) styrene or styrene derivatives as a reactive diluent (3) paraffin as a styrene emission inhibitor and an adhesion promotor present in an amount sufficient to increase the adhesion characteristics of the VER composition with a reinforcing material used therewith, characterized in that the adhesion promotor is a drying oil, soluble at least in part both in the vinylester resin and in the paraffin wax. The present invention stems from the discovery of the benefits of a drying oil, soluble at least in part both in the vinyl ester resin and in the paraffin wax, as an adhesion promoter in a VER composition wherein the styrene emission has been inhibited by the presence of paraffins in the VER composition. The VER composition is improved by the addition of an adhesion promoter in the form of a drying oil soluble at least in part both in the vinyl ester resin and in the paraffin wax. The present invention also provides a desirable low styrene emission VER composition which is capable of utilization in the fabrication of a range of fiber reinforced plastic structures and equipment. For the purpose of this invention, unless otherwise distinguished, the term "VER composition" means a composition comprising a VER, a reactive diluent, a styrene emission inhibitor and a drying oil as an adhesion promoter. The VER herein is an esterification product of a polyepoxide and a monounsaturated monocarboxylic acid. An early patent, US-A-3,179,623, describes the above reactions and resins. Further details about the resins and conditions and methods of making them can be found in the following US-A-3,301,743; 3,317,465; 3,377,406; 3,256,226 and 3,367,992. An example of the said VER includes that VER sold by The Dow Chemical Company under the trademark Derakane®. During the fabrication of various end products from a VER it is desirable to reduce the viscosity of the VER in order to facilitate the processing. A reactive diluent is utilized to reduce the viscosity of the VER. Generally, the reactive diluent is present in amounts ranging from 25 to 55 weight percent of the VER composition depending on the monomer selected, other additives employed and other factors. Typical reactive diluents include, for example, styrene, vinyl toluene, halogenated styrenes, alkyl substituted styrenes. Other diluents which may be present are acrylic and methacrylic esters, and hydroxylalkyl esters of acrylic and methylacrylic acid. Most preferably, the reactive diluent is styrene. The physical properties of the VER composition comprising a VER and a reactive diluent may be modified by adding various materials to the resin. For example, inert reinforcing materials such as glass fibers and inert fillers such as calcium carbonate or kaolin clay are both commonly employed to improve physical properties of the VER composition and reduce costs. The volatility of the reactive diluent, such as styrene, results in the emission of styrene vapor from the VER composition. The present composition employs a film-forming additive, i.e., paraffin wax, to inhibit the emission of styrene into the work atmosphere. The paraffin wax is preferably utilized in amounts ranging from 0.1 to 5 weight percent of the said VER composition. Most preferably, in amounts ranging from 0.25 to 0.5 weight percent of the VER composition. Preferably, paraffin wax, having an average melting point of 52°C, is utilized. The utilization of a paraffin wax as a film-forming inhibitor results in effective inhibition of styrene emission. However, a drawback of the use of the paraffin wax in the fiber-reinforced VER compositions is the undesirable loss of adhesion bond strength between the fiber fillers and the VER composition. Such adhesion bond strength is qualitatively measured by examining the amount of fibers present in the break pattern of a VER laminate that has been separated. In other words, the more fibers present in the break surface, the better the adhesive bond strength of the VER composition. Where the break surface is clean, i.e., very few glass fibers, the adhesive bond strength is poor. It has been found that the utilization of a drying oil results in a low styrene emission VER composition which exhibits desirable adhesive bond strength to the glass fibers. The drying oils are generally catagorized by iodine value. The iodine value, which is the measure of the proportion of unsaturated bonds present, is 140 or greater for drying oils. The number represents the percentage of iodine (i.e., grams per 100 grams) absorbed by a substance. The drying oils are preferably glycerides, i.e. esters of the trihydric glycerol and unsaturated fatty acids such as linoleic and linolenic acids. The glyceride is preferably linseed oil. More preferably, the glyceride is raw or boiled linseed oil. Linseed oil is produced from the seeds of the common flax plant. The approximate percent chemical composition of commercial fatty acids in linseed oil are as follows: (a) saturated fatty acids; myristic 1 percent, palmitic 7 percent and stearic 2 percent; and (b) unsaturated fatty acids: oleic 23 percent, linoleic 17 percent and linolenic 51 percent. See Kirth-Othmer, Encyclopedia of Chemical Technology, Vol. 4, 3rd Ed., p. 848 (1978), and generally, Vol. 8, 3rd Ed., pp. 130-150. Linseed oil can include raw, boiled, double-boiled, blown, alkali-refined, acid-refined and heat-polymerized species. The unsaturation of the fatty acids, primarily linoleic and linolenic acids, gives the linseed oil its reactivity and drying properties. Linseed oil dries to a characteristic film and polymerizes on exposure to air. Linseed oil has been used in paints, varnishes, putty, alkyd resins, urethane oils, printing inks, soap, and coating for electrodeposition. It is preferable to have the said drying oil present in an amount sufficient to increase the adhesion characteristic of a VER composition with a reinforcing material used therewith. Such an amount ranging from 0.1 to 5 preferably from 0.1 to 0.5 weight percent of the VER composition and most preferably in an amount ranging from 0.25 to 1 weight percent of the VER composition. The VER composition of this invention shows improved adhesion bond strength as compared to the low styrene emission VER base which does not contain a drying oil as an adhesion promoter. Such VER compositions are useful in fabricating a range of fiberreinforced plastic structures and equipment by all fabricating methods. The following example is provided to illustrate the invention but is not intended to limit the scope thereof. All parts are percentages by weight unless otherwise indicated. Example 1 A multilayer laminate was prepared from Derakane® 411-45 using the following composition: Derakane® 411-45 is a vinyl ester resin sold by The Dow Chemical Company. The resin was prepared by first blending a diglycidyl ether of bisphenol A having an epoxy equivalent weight of 188 and a diglycidyl ether of bisphenol A having an epoxy equivalent weight of 535. Added to this reaction product were glacial methacrylic acid, tris(dimethylaminomethyl)phenol and hydroquinone. Then maleic anhydride was added and reacted until the carboxylic acid content was 1 percent. Then parts of styrene containing 50 parts per million tertiary butyl catechol were added and mixed with the reaction products. The Derakane® 411-45 contains 45 percent monomeric styrene. Other Derakane® vinyl ester resins that can be used include: Derakane® 411-C-50 resin containing 50 percent monomeric styrene; Derakane® 470-45 resin containing 45 percent monomeric styrene; and Derakane® 510-A-40 resin, a brominated, vinyl ester resin containing 40 percent monomeric styrene. A three layer 12 inch by 12 inch (30.48 cm by 30.48 cm) laminate was prepared containing 128 grams (g) (30 percent) of glass fibers and 300 g of the above composition cured with 0.9 g of cobalt naphthenate (6 percent), 0.15 g of dimethylaniline and 3 g of methylethylketone peroxide (60 percent). In the above composition, the Derakane® 411-45 contained 45 percent styrene, and the additional 4.25 weight percent styrene was used to dissolve the wax and linseed oil. The styrene loss was measured by the amount of weight loss of the three-ply laminate over the period of time required for complete curing. The above laminate was found to lose 9.3 g of styrene. After the determination of the styrene loss, another three layers were added to the original laminate. The first three layers of laminate were partially separated from the second three layers of laminate by a strip of polyester film. Such a strip of polyester facilitates the prying apart of the layers in order to provide a break surface from which the adhesion bond strength may be qualitatively measured. The laminate was allowed to fully cure before it was pryed apart. The degree of adhesion bond strength between the glass fibers and the resin is judged by the amount of glass fibers present in the break pattern. The test was run on four laminates prepared in the same manner as discussed above. The more glass fibers which are present in the break surface the better the adhesion bond strength of the resin to the glass fibers. Where the break is clean, i.e., where there are very few glass fibers present, the adhesion bond strength is poor. The results are summarized below in Table I. Example 2 A similar three-ply laminate, using 0.1 weight percent paraffin wax P58 and 0.5 weight percent boiled linseed oil was prepared similarly as described hereinabove in Example 1. The styrene loss was measured as discussed in Example 1 and was found to be 7.5 g. The adhesion bond strength between the glass fibers and the resin was judged by the method of Example 1. The results are summarized in Table I. Example 3 A similar three-ply laminate, using 0.1 weight percent paraffin wax P67 and 0.5 weight percent boiled linseed oil was prepared similarly as described hereinabove in Example 1. The styrene loss was measured as discussed in Example 1 and was found to be 6.9 g. The adhesion bond strength between the glass fibers and the resin was judged by the method of Example 1. The results are summarized in Table I. Comparative Example A A similar three-ply laminate, less the paraffin wax and linseed oil, was prepared similarly as described hereinabove in Example 1. The styrene loss was measured as discussed in Example 1 and was found to be 17.7 g. The results are summarized in Table I. Comparative Example B A similar three-ply laminate, less the linseed oil, was prepared similarly as described hereinabove in Example 1. After complete curing another three layers of the instant composition were added to the original laminate as in Example 1. The styrene loss was measured as discussed in Example 1 and was found to be 9.3 g. The adhesion bond strength between the glass fibers and the resin was judged by the method of Example 1. The results are summarized in Table 1. Comparative Example C A similar three-ply laminate, less the linseed oil, was prepared with 0.25 weight percent paraffin wax P58 similarly as described hereinabove in Example 1. After complete curing, another three layers of the instant composition were added to the original laminate as in Example 1. The styrene loss was measured as discussed in Example 1 and was found to be 5.4 g. The adhesion bond strength between the glass fibers and the resin was judged by the method of Example 1. The results are summarized in Table I. Comparative Example D A similar three-ply laminate, less the linseed oil, was prepared with 0.25 weight percent paraffin wax P67 similarly as described hereinabove in Exampie 1. After complete curing, another three layers of the instant composition were added to the original laminate as in Example 1. The styrene loss was measured as discussed in Example 1 and was found to be 7.5 g. The adhesion bond strength between the giass fibers and the resin was judged by the method of Example 1. The results are summarized in Table I. The results indicate Applicant's VER composition exhibits low styrene emission and excellent adhesion bond strength between the VER composition and the giass fibers. The addition of the linseed oil improves the adhesion bond strength between the VER composition and the glass fibers, while effectively maintaining low styrene emission for the VER compostion. Example 4 A similar three-ply laminate, using 0.1 weight percent boiled linseed oil TE-37 and 0.25 weight percent paraffin wax P52, was prepared similarly as described hereinabove in Example 1. The styrene loss was measured as discussed in Example 1 and was found to be 9.6 g. The adhesion bond strength between the glass fibers and the resin was judged by the method of Example 1. The results are summarized in Table II. Example 5 A similar three-ply laminate, using 0.3 weight percent boiled linseed oil TE-37 and 0.25 weight percent paraffin wax P52, was prepared similarly as described hereinabove in Example 1. The styrene loss was measured as discussed in Example 1 and was found to be 9.9 g. The adhesion bond strength between the glass fibers and the resin was judged by the method of Example 1. The results are summarized in Table II. The results in Table II indicate that the concentration of linseed oil does not appreciably affect the amount of styrene lost from the VER composition. However, the linseed oil concentration does affect the adhesion bond strength between the VER composition and the glass fibers. The adhesion bond strength is improved as the linseed oil concentration increases. Example 6 A similar three-ply laminate, using 0.5 weight percent raw linseed oil TE-1 and 0.25 weight percent paraffin wax P52, was prepared similarly as described in Example 1. The styrene loss was measured as discussed in Example 1 and was found to be 8.7 g. The adhesion bond strength between the glass fibres and the resin was judged by the method of Example 1. The results are summarized in Table III. Example 7 A similar three-ply laminate, using 0.5 weight percent boiled linseed oil TE-37 and 0.25 weight percent paraffin wax P52, was prepared similarly as described in Example 1. The styrene loss was measured as discussed in Example 1 and was found to be 8.4 g. The adhesion bond strength between the glass fibers and the resin was judged by the method of Example 1. The results are summarized in Table III. The results in Table III indicate that both raw and boiled grades of linseed oil improve the adhesion bond strength between the VER composition and the glass fibers, while effectively maintaining low styrene emission for the VER composition. The boiled linseed oils have a slightly better peel adhesion rating than the raw linseed oils. Example 8 A similar three-ply laminate, using 95 weight percent Derakane® 510-A-40, 0.5 weight percent boiled linseed oil TE-3 and 0.25 weight percent paraffin wax P52, was prepared similarly as described hereinabove in Example 1. The styrene loss was measured as discussed in Example 1 and was found to be 6.6 g. The adhesion bond strength between the glass fibers and the resin was judged by the method of Example 1. The results are summarized in Table IV. Example 9 A similar three-ply laminate, using 95 weight percent Derakane® 411-C-50, 0.5 weight percent boiled linseed oil TE-37 and 0.25 weight percent paraffin wax P52, was prepared similarly as described hereinabove in Example 1. The styrene loss was measured as discussed in Example 1 and was found to be 14.1 g. The adhesion bond strength between the glass fibers and the resin was judged by the method of Example 1. The results are summarized in Table IV. Example 10 A similar three-ply laminate, using 95 weight percent Derakane® 47u-45, 0.5 weight percent boiled linseed oil TE-37 and 0.25 weight percent paraffin wax P52, was prepared similarly as described hereinabove in Example 1. The styrene loss was measured as discussed in Example 1 and was found to be 7.2 g. The adhesion bond strength between the glass fibers and the resin was judged by the method of Example 1. The results are summarized in Table IV. The results in Table IV indicate that linseed oil improves the adhesion bond strength between the various VER compositions and the glass fibers, while effectively maintaining low styrene emission for the various VER composition.

Claims: Low styrene emission, VER composition containing (1) a VER which is an esterification product of a polyepoxide and a monosaturated monocarboxylic acid, (2) styrene or styrene derivatives (ie. vinyl toluene, halogenated styrenes and alkyl substituted styrenes) as a reactive diluent (3) paraffin as a styrene emission inhibitor and an adhesion promotor present in an amount sufficient to increase the adhesion characteristics of the VER composition with a reinforcing material used therewith, characterized in that the adhesion promotor is a drying oil, soluble at least in part both in the vinylester resin and in the paraffin wax. The VER composition of Claim 1 wherein said drying oil is a glyceride. The VER composition of Claim 2 wherein said glyceride is linseed oil. The VER composition of Claim 3 wherein said linseed oil is raw linseed oil or boiled linseed oil. The VER composition of Claim 3 wherein said linseed oil is 0.1 to 5 weight percent of said VER composition. The VER composition of Claim 3 wherein said linseed oil is 0.25 to 1 weight percent of said VER composition. The VER composition of Claim 1 wherein said drying oil is 0.1 to 0.5 weight percent of said VER composition. The VER composition of Claim 1 wherein the said paraffin wax is 0.1 to 5.0 weight percent of said VER composition. The VER composition of Claim 1 wherein the said paraffin wax is 0.25 to 0.5 weight percent of said VER composition. The VER composition of Claim 1 wherein said paraffin is a paraffin wax P52 which has a melting point of 52°C. Claims for the following Contracting State : AT A process for making a low styrene emission, VER composition by processing (1) a VER which is an esterification product of a polyepoxide and a monounsaturated monocarboxylic acid, (2) styrene or styrene derivatives (i.e. vinyl toluene, halogenated styrenes and alkyl substituted styrenes) as a reactive diluent. (3) paraffin as a styrene emission inhibitor and an adhesion promotor present in an amount sufficient to increase the adhesion characteristics of the VER composition with a reinforcing material used therewith, characterized in that the adhesion promotor processed therein is a drying oil, soluble at least in part both in the vinyl ester resin and in the paraffin wax. The process of Claim 1 wherein said drying oil is a glyceride. The process of Claim 2 wherein said glyceride is linseed-oil. The process of Claim 3 wherein said linseed oil is raw linseed oil or boiled linseed oil. The process of Claim 3 wherein said linseed oil is 0.1 to 5 weight percent of said VER composition. The process of Claim 3 wherein said linseed oil is 0.25 to 1 weight percent of said VER composition. The process of Claim 1 wherein said drying oil is 0.1 to 0.5 weight percent of said VER composition. The process of Claim 1 wherein the said paraffin wax is 0.1 to 5.0 weight percent of said VER composition. The process of Claim 1 wherein the said paraffin wax is 0.25 to 0.5 weight percent of said VER composition. The process of Claim 1 wherein said paraffin is a paraffin wax P52 which has a melting point of 52⁰C.

Inventors: SCHOLS, JOHN AREND, YU, KEECHUNG
Applicants: THE DOW CHEMICAL COMPANY
Application year: 1986
Main classification: C08F299
IPC codes: C08K5, C08F299