Description

The present invention relates to the development of a dual functional additive system for theπroset polyester resins which imparts improved glass read out, enhanced pigrentability and superior low shrink properties over the known prior art, thereby producing an overall improved Class A quality surface finish for thermoset polyester resin products. Further, the dual functional additive of the present invention is compatable with other conventional low shrink additives as may be added to the theπroset polyester resin, and may or may not be used with them, a significant improvarent in dynamic impact properties is obtained over that exhibited by any of the known prior art.

The dual functional additive systβr comprises the dual thickening systar comprised of iretallic oxides and hydroxides of calciun or iragiesium as described in Epel et al, U.S. Patent No. 4,067,848 and incorporated herein by reference, and an additional isocyanate terminated urethane prepolymer which has an NCO/CH ratio within the range of approximately 1.21 to approximately 5/1 and preferably an NOO/CH between 1.8 to 3.

The dual functional additive systar provides that the isocyanate terminated urethane prepolymer becomes covalently bonded to the theπroset polyester resin matrix of the polyester resin product. It should be arphasized that, insofar as is known, none of the conventional low shrink additives contained within the prior art covalently bonds with the theπroset polyester resin material. Ey virtue of being covalently bonded to the ther oset polyester resin, the new additive imparts improved dynamic impact properties to the thermoset polyester resin product.

Finally, this new isocyanate terminated urethane additive, when used in conjunction with the teachings of Epel et al, serves a dual purpose as a low shrink additive to allow greater predicability of so-called "shrinkage" during formation of theπroset polyester resin

material products, and aids in the thickening process during maturation.

Low shrink additives comprised of a polyisocyanate and a polyether polyol for use in thermoset polyester resin products to minimize shrinkage experienced by the theπroset polyester resin product during final cure are old and well known in the prior art.

The present invention relates to the development of a dual functional additive for use in thermoset polyester resin products incorporating the dual thickening system of Epel et al, and comprises an isocyanate terminated urethane prepolymer additive based upon a polyioscyanate and a polyether or polyester polyol, and preferably a polyether polyol, which acts in concert with N00, etc. to thicken the systβp and impart improved viscosity index to the polyester matrix as explained in Epel et al's patent, and, at the same time, imparts superior dimensional change predictability to the thermoset polyester resin product during final cure than would otherwise be obtainable by using the dual thickening systar of Epel et al.

Further, by virtue of the fact the dual functional additive of the present invention covalently bonds to the theπroset polyester resin, the resulting product possesses improved dynamic impact properties than would otherwise be expected frc using any of the conventional low shrink additives of the prior art alone, as well as superior high tarperature property retention.

The isocyanate terminated urethane prepolymer of the present invention is made in a one-step process and has an NOO/CH ratio of approximately 1.2/1 to approximately 5/1, and preferably an NCO/C8 ratio of 1.8 to 3 and is made by combining one equivalent of a polyol, preferably polyether polyol having a molecular weight of approximately 600 to 4,000 and a functionality of approximately 2 to 3, and preferably 2, with two equivalents of a polyisocyanate and preferably a di-isocyanate and 0 to 1% of any conventional urethane catalyst, such as

stannous octoate, dibutyltin dilaurate (and the like), said amount to vary according to the total weight of the urethane. This dual functional additive may or may not be dissolved in a ethylinically unsaturated monomer, such as styrene.

As previously mentioned, this dual functional additive is contemplated for use with the dual thickening systar of Epel et al to aid in the thickening process and improve viscosity index, and by virtue of the fact tnat the additive is isocyanate terminated, covalent bonding to the thermoset polyester resin material is facilitated, thereby enhancing the dynamic impact properties of the theπroset polyester resin material. Finally, the use of this additive allows greater predictability of dimensional changes to be expected from the thermoset polyester product during final cure than is otherwise obtainable, insofar as is known, frαr any of the conventional low shrink additives of the prior art.

PRIOR ART STATEMENT

Epel et al, U.S. Patent No. 4,067,845 describes a dual thickening systar tor use in the production of a moldable thermoset polyester resin composition. ϋie dual thickening systar as taught by • Epel at al is an oxide or hydroxide of calcium or magnesium, and preferably magnesium, and is used in conjunction with a polyisocyanate to impart improved molding characteristics to the thermoset polyester resin than would otherwise be obtained from using only oxides and/or . hydroxides of calcium and magnesium.

Epel el al differs from the present invention by reason that tne polyisocyanate specified in Epel et al does not include an isocyanate terminated urethane prepolymer based upon a polyester polyol or a polyether polyol or a mixture thereof and a polyisocyanate. The dual functional additive systar of the present invention deletes the organic polyisocyanate of Epel et al, and instead substitutes from the dual thickening systar of Epel et al, an isocyanate terminated urethane prepolymer based upon a polyether polyol or a polyester polyol or a

ixture thereof, to impart better low shrink predictability than would otherwise be expected frc using the system as taught by Epel et al alone, while acting as a thickener for improved molding characteristics.

Moreover, the disclosure of Epel et al does not address itself specifically to the problar of predictability of shrinkage to be experienced by the final product discussed in Epel et al.

O'Connor et al. U.K. Patent No. (33 2045259B discloses a urethane dominated low shrink additive for use in thermoset polyester resin products. The low shrink additive is based upon a polyester or polyether polyol or mixture thereof, preferably a polyether polyol, a polyisocyanate, and an isocyanate reactive unsaturated monomer, preferably ϊydroxyalkylacrylate, whereby the CH groups of the monomer react with the NCO groups on the intermediate prepolymer based on the polyether polyisocyanate thereby "capping off" the NGO and exposing a double bond for later reaction.

The urethane low shrink additive of O'Connor et al is made in a two-step process. Specifically, an isocyanate terminated prepolymer is made based upon either a polyether polyol or a polyester polyol as outlined above, and a polyisocyanate whereby an isocyanate terminated prepolymer is created having a ratio of NCO/CH of approximately 1.02/1 to approximately 1.6/1 and preferably 1.1/1 to 1.4/1. The isocyanate groups are then reacted with an isocyanate reactive unsaturated monαrer selected from among suitable esters, amides or alcohols, and preferably with hydroxethyl acrylate. ϊhis reaction should result in a final free NCO content preferably in the range of 0 - 1% and most preferably in the range or 0 - .5% of free NGO. The reaction of the isocyanate terminated prepolymer with the unsaturated mon rer described above results in a controlled molecular weight oligomer with terminal unsaturation. The additive as described in O'Connor et al is a low shrink additive and does not, in stark contrast to the present invention, take part in the thickening process using the dual thickening system as described in Epel

et ai.

Moreover, the dual function additive isocyanate terminated urethane polymer of the present invention does not provide terminal unsaturation, as does the low shrink additive of O'Connor et al.

Rather, the dual functional additive of the present invention is terminated by NGO groups which react with the terminal CH groups of a thermoset polyester resin and covalently bond thereto, to provide low shrink advantages and higher impact properties, as will be described herein, and in conjunction with the dual thickening systar of Epel et al, act as a thickener for the thermoset polyester resin for improved molding characteristics. The lew shrink additive as described in O'Connor et al depends upon reactions with the terminal reactive unsaturation of the prepolymer for its low shrink properties. Further, the present invention provides for an NGO/OH ratio of approximately 1.2/1 to approximately 5/1, and preferably an NGO/OH ratio between 1.8 to 3. Thus, the mechanisms of the reaction of the respective low shrink additives are vastly different.

O'Connor et al, Euroean Patent Application 0074746 relates to a thermosetting polyester resin composition which includes a select polyurethane oligomer to improve impact properties and surface characteristics of the theπroset polyester resin composition. These polyester resin systars as arbodied in O'Connor et al 0074746 give increased impact properties as well as low shrink characteristics to the polyester resin system.

Hcwever, the manner in which these ends are achieved differs from the present invention. Specifically, polyurethane chemical system arployed by O'Connor et al is formed by the reaction of a hydroxyl terminated prepolymer with dicarboxylic acid anhydrides. The present invention does not use dicarboxylic acid anhydrides to form the prepolymer of the present invention. Moreover, the NGO/CH ratio of the polyurethane oligemer of O'Connor et al is about .3/1 to about .99/1 whereas in the present invention, the NGO/CH ratio is from between 1.2/1

to about 5/1 and preferably 1.8/1 to about 3/1. The systar as defined by

O'Connor et al would give rise to fiber readout problems which are overcome in the present invention.

In addition, O'Connor et al arphasizes the use of chain extenders to lengthen the prepolymer of his invention. The average molecular weight of the polyol used in O'Connor et al is about 300 to about 10,000, which is different than the present invention wherein the range of 600 to 4,000 is preferred. Further, O'Connor et al prefers a polyester polyol whereas in the present invention, polyether polyols are the preferred polyol reactants. In addition, the polyurethane oligcmer that is utilized according to the invention in O'Connor et al is a hydroxy terminated prepolymer whereas in the present invention, the prepolymer is isocyanate terminated. Further, the polyurethane oligomer of O'Connor et al is reacted with a dicarbo^-lic acid whereas in the present invention, such is not the case.

Finally, the present invention is contarplated for use with the dual thickening systar of Epel et al to aid as a thickener as well as a low shrink additive to form a thermoset polyester resin product having good low shrink characteristics and dynamic impact properties, whereas, O'Connor et al cannot, because of the hydroxyl termination of the prepolymer to be used with Epel et al. Thus, the present invention differs rro O'Connor et al.

O'Connor et al. U.S. Patent 4,424.333 relates to the modified polyurethane liquid polymer composition comprised of a polyurethane oligomer containing terminal ethylenic unsaturation. The polyurethane oligomer contarplated by O'Connor et al is prepared by reacting an organic polyisocyanate and a polyether polyol to form an oligomer and then reacting this product with an isocyanate reactive group containing an unsaturated monomer selected frc appropriate acrylates and acrylαrides or mixtures thereof, and preferably bydrojyethylacrylate to produce the terminal unsaturation.

Bie polyol used should have an average molecular weight of approximately 75 to approximately 500, and preferably 100 to 200, and a functionality of at least 3, and preferably 3 - 8 and most preferably 4 - 6. The ratio of NCO/CH in the polyurethane oligomer of O'Connor et al is approximately .8/1 to approximately 2/1 and preferably 1/1 to about 1.2/1. It is believed that, aside from the differences in molecular weight and NGO/CH ratios, the polyurethane oligemer of O'Connor et al cannot be used with the dual thickening systar of Epel et al.

As previously stated, the present invention is a dual functional additive which aids the dual thickening system of Epel et al and covalently bonds to the themoset polyester resin of such a product to present predictability of dimensional changes of such a product during final cure such as could not be expected by the use of Epel et al alone. O'Connor et al cannot, because of its ethylenic terminal unsaturation, aid the dual thickening systar of Epel et al. Further, the polyether polyol contarplated for use with the present invention has a molecular weight of approximately 600 to 4,000, a functionality of 2 to 3, and preferably 2, and an NCO/CH ratio, after rection to form the isocyanate terminated urethane prepolymer of the present invention of 1.2/1 to 5/1, and preferably an NCO/CH ratio between 1.8 and 3. Thus, the present invention differs trcm O'Connor et al.

DETAILED DESCRIPTION OF PREEΕRRED EMBCDIMENT

The isocyanate terminated urethane prepolymer of the present invention is based upon a polyether or polyester polyol, or a mixture thereof, and preferably a polyether polyol, and a di-isocyanate or polyisocyanate. The polyol is preferably a dio or triol having a molcular weight of approximately 600 to approximately 4,000, and preferably about 2,000, as exemplified fcy BASF's Pluracol P-2010, and a functionality of approximately 2 to approximately 6, and preferably 2 to 3 and more preferably 2. Ωie dual functional additive of the present invention is formed in a one-step addition reaction between one equivalent weight of the polyol as described above and two equivalent weights ot the polyisocyanate in the presence of approximately 0 - 1% of a conventional urethane catalyst such as stanneous octoate, dibutyltin dilaurate and the like, and the amount of such catalyst is determined according to the total weight of the urethane.

The isocyanate terminated urethane additive thus formed should have an isocyanate to bydroxyl ratio NCO/CH of approximately 1.2/1 to approximately 5/1, and preferably NGO/OH between 1.8 to 3, and most preferably about 2.

The dual functional additive of the present invention is contemplated for use with themoset polyester resin products to which it is covalently bonded to provide improved dynamic impact qualities such as could not be expected, insofar as is known, with any low shrink additive contained within the prior art. In addition, this additive provides greater "low shrink" predictability than would otherwise be expected from any of the conventional low shrink additives contained within the known prior art. Further, by replacing the organic polyisocyanate of Epel et al with the isocyanate terminated urethane prepolymer of the present invention, the additive acts as a thickener for the theπroset polyester resin to wnicn it is added, rendering the matured paste to have improved molding characteristics.

The isocyanate terminated urethane prepolymer is prepared by first reacting an organic polyisocyanate, and preferably a di-isocyanate with a polyol, using standard procedures to yield an isocyanate terminated prepolymer of controlled molecular weight and having an NCD/CH ratio of approximately 1.2/1 to approximately 5/1, and preferably NGO/OH between 1.8 to 3, and most preferably about 2.

The polisocyanates used in the formation of the present invention include tuluene di-isocyanate, such as the 80:20 or 65:35 iso er mixture of the 2,4- and 2,6 isαreric forms, ethylene di-isocyanate, propylene di-isocyanate, eta and para phenyl di-isocyanates, 4,4'-diphenyl methane di-isocyanate (MDI) or a mixture of MDI and its trifunctional cyclic adduct products containing carbiodii ide linkages, 1,5 napthalene di-isocyanate, para and meta xylene di-isocyanates, alkylene di-isocyanates such as tetra ethylene di-isocyanate and hexametiylene di-isocyanate, 2,4- and 2,6 di-isocyanate methylcyclohexane, dicyclcexylmethane di-isocyanate, and polymeric MDI containing an average of from two isocyanate groups per molecule. Other polyisocyanates which may be employed include polyisocyanate of toluene di-isocyanate, polyisocyanate prepolymers of aromatic type, toluene di-isocyanate based adducts, arcmatic/aliphatic polyisocyanates and polyfunctional aliphatic isocyanate. The exact polyisocyanate employed is not critical, but di-isocyanates are preferred, and of these, 4,4' diphenyl methane di-isocyanate (MDI) or a mixture of MDI and its trifunctional cyclic adduct products containing carbodiimide linkages are preferred. It should be noted that differing results in respect to low shrinkage additives will be obtained by the use of different polyisocyanates and it must be emphasized that di-isocyanates are preferred.

The polyol reactant used in the dual functional additive is selected from either a polyester polyol or polyether polyol, preferably polyether polyols and mixtures of two or more such polyether polyol compounds. The polyol reactant, or mixture thereof, used has an average

equivalent weight of between 600 to 4000 and a functionality of between 2 and 6, and preferably 2 to 3 and more preferably 2.

Among suitable polyether polyols, it is contarplated that polyoxyalkylene polyols and mixtures thereof may be used. These can be prepared according to well known methods, by condensing an alkylene oxide, or mixture of alkylene oxides using random or stepwise addition, with a polyhydric initiator or a mixture of polybydric initiators.

The alkylene oxides contarplated for use include ethylene oxides, propylene oxide, butylene oxides, arrylene oxide, aralkylene oxides, such as trichlorobultylene oxide and such, and the most preferred alkylene oxide is propylene oxide or a mixture thereof with ethylene oxide using random or stepwise ojyalkylation.

Polybydric initiators used in preparing the polyether polyol reactant include (a) aliphatic diols such as ethylene glycol, 1,3-propylene glycol, 1,2-propylene glycol, butylene glycols, butane diols, pentane diols and the like, (b) the aliphatic triols such as glycerol, trimethylolpropane, triethylolpropane, trimethylolhexane and the like, (c) the polyamines such as tetraettylene diamine and (d) the alkanolamines such as diethanolamine, triethanola ine, and the like. Preferably, the polyfcydric initators of choice for use in preparing the polyether polyol reactant is an aliphatic diol or triol such as ethylene glycol, propylene glycol, glycerol, trimethylolpropane and the like.

If a polyester polyol is selected for use as the polyol reactant of the dual functional additive of the present invention, such a polyol is usually formed by reacting a polycarboxilic acid with a polybydric initiator, such as a diol or triol. The polycarboxylic acids include oxalic, malonic, succinic, glutaric, adipic, pimelic, subelric, azelaic acid, and the like. Illustrative polyhydric alcohols include various diols and triols and higher functionality alcohols such as ethylene glycol, 1,3-propylene glycol, 1,2-propylene glycol, butylene glycols, butane diols, pentane diols, glycerol, trimethylolpropane.

trimethylolhexane, hexane 1,2,6-triol and the like.

When a polyether polyol reactant is to be created by the alkylene oxide polylydric initiator reaction, usually a catalyst such as KCH, as is well known in the prior art, is added to speed up the reaction. The resulting polyether polyol should have an average molecular weight of approximately 600 to 4,000. After reaction, the catalyst is preferably removed, leaving a polyether polyol suitable for reaction with the polyisocyanate reactants as discussed above to form the isocyanate terminated urethane prepolymer of the present invention.

In forming the isocyanate terminated urethane prepolymer which comprises the present invention, one equivalent weight of the polyol reactant as defined above is reacted with 1.2 to 5, and preferably two equivalent weights of a polyisocyanate as defined previously in the presence of any conventional urethane catalysts such as stannous octoate and dibutyltin dilaurate and the like, whereby the isocyanate groups are placed on the terminal ends of the prepolymer, thereby yielding the isocyanate terminated urethane prepolymer of the present invention. It should be noted tbat the prepolymer may be made in the presence of an ethylinically unsaturated monomer, such as styrene, or that a monomer may be added to it after it has been made without adversely affecting its function as a low profile additive to impart the advantages described herein.

The isocyanate terminated urethane prepolymer additive of the present invention may or may not be used with any of the conventional low shrink additives of the prior art, such a polyvinyl acetate and polymethyl methacrylate or a mixture thereof, or any other linear oligomer having a molecular weight within the range of approximately 10,000 to approximately 90,000.

Moreover, regardless of whether or not the prepolymer of the present invention is used with a conventional low shrink additive, the ratio of the total amount of prepolymer to polyester resin should

opti ally be within the range of approximately 10 parts by weight of prepolymer to 90 parts by weight of polyester resin, to approximately 60 parts by weight of prepolymer to 40 parts by weight of polyester resin.

Die SMC contarplated for use with the present invention is comprised essentially of the following ingredients: (a) an unsaturated polyester resin having (1) a ratio of hydroxyl groups to carboxyl groups of between 5.7 and 8.2, and (2) an acid number of at least 14, and (3) an average molecular weight between about 800 and 5,000; (b) a dual thickening systar comprised of the isocyanate terminated urethane prepolymer of the present invention in an amount sufficient to react with at least 10 percent, but not more than 105 percent of the hydroxyl groups present, and a metallic oxide or iydroxide selected frσm Group IIA of the periodic table and consisting of calciur and magnesium oxides or hydroxides in an amount to react with at least 30 percent, but not more than 75 percent of the carbojyl groups present; (c) an ethylinically unsaturated monomer and a free radical polymerization catalyst; (d) an inert filler; (e) fiberous reinforcing material; and (f) a mold release agent.

When used in an SMC as defined above, the isocyanate terminated urethane prepolymer additive of the present invention, the prepolymer may be dissolved in styrene and then used like any other low shrink additive, and is employed in an amount sufficient to react with at least 10 percent but not more than 105 percent of the hydroxyl groups present in the reaction.

The metallic oxide or hydroxide used in the dual thickening systar is essentially a metal oxide or hydroxide from the Group IIA on the periodic table and comprises calcium or magnesium. Althouφ calcium may be used in its various oxides and hydroxides, the magnesium is preferred inasmuch as superior results are achieved by the use of magnesium. Althouφ the present invention may be used alone, it may also be used with a monomer from the group styrene, vinyl toluene and vinyl

acetate and any other ethylinically unsaturated monomer and when so used, is ordinarily present in an amount to give .5 to 2.5 moles of monomer unsaturation per mole of unsaturation in the unsaturated polyester resin. Styrene and vinyl toluene are preferred monomers, althouφ others may be used.

A free radical polymerization catalyst is also employed in the present invention. The catalyst is preferably present in an amount of .1 part per 100 parts of total resin and monomer, the parts being measured by weiφt. The free radical polymerization catalyst is added to the uncured composition so that upon heating to the activation temperature, the additive type cross-linking polymerization reaction will commence between the polymerizable monomer and the unsaturated polyester resin to form the matrix previously described. The catalyst is usually employed in an amount in the range of about .1 to 3.0 parts per 100 parts of the total monαrer and resin and is usually a peroxide.

The mold release agent contarplated in the present invention may be any of those used in the prior art, such as zinc stearate, calcium stearate, magnesium stearate, organic phosphate esters and other organic liquid internal mold release agents.

The reinforcing fibers are usually present in an amount of about 10 to 70 weight percent for sheet molding compositions and is preferably fiberglass. The preferred range for this reinforcing fiber is approximately 15 to 70 weiφt percent for use in thermoset polyester resin applications, such as an SMC.

Any number of nonreinforcing fillers may be added to the composition to reduce overall material costs without sacrificing a significant degree of the desirable physical properties in the final product, or may be added to impart specific properties to the uncured compound. Any number of fillers may be used in an amount ranging from about 20 parts to 1000 parts by weight per 100 parts of the pure polyester resin in thermoset polyester resin applications, such as an

-U-

SMC.

In addition, the invention may, as previously stated, include a low shrink additive polymer, which is ordinarily dissolved in the same type of ethylinically unsaturated monαrer in which the polyester resin is dissolved.

In use of the dual functional additive of the present invention with themoset polyester resin products as defined in Epel et al, and especially sheet molding compositions (SMC) , the unsaturated polyester resin as described in Epel et al is dissolved in a monomer such as styrene, vinyl acetate or vinyl toluene. The dual thickening systar of Epel et al is modified by the replacement of the organic polyisocyanate defined therein with the dual functional additive of the present invention. A free radical catalyst, which is activated by heat such as organoperoxides, hydroperoxides or azo compounds, and usually a peroxide, is added to the polyester resin material. Inert fillers may be added to reduce the overall cost of the SMC wljile not appreciably sacrificing the essential properties of the SMC. The modified dual thickening systar is then added to the polyester resin, along with an additional amount of the isocyanate terminated urethane prepolymer of the present invention in an amount such that the total amount of prepolymer to polyester resin is within the range of approximately 10 part by weiφt of prepolymer to 90 parts by weiφt of polyester resin material to approximately 60 parts by weight of prepolymer to 40 parts by weiφt of polyester resin.

Reinforcing fibers, such as fiberglass, are added to the SMC in a conventional manner. Once the fibers have been thoroughly admixed with the composition, the SIC is B-staged to a moldable consistency by aging at 90 to 104° F for 3 to 5 days. After the material has been B-staged, it can be molded at 280 to 315° F in 1 to 2 minutes, depending on the specific configuration, i.e. thickness, of the part being molded. After B-staging has occurred, the SMC may be stored for long periods of time without jeopardizing either its handleability or processability.

Finally, by virtue of being covalently bonded to the polyester resin matrix of the SMC, the new additive imparts superior temperature retention properties to the SIC infrastructure which are not achievable, insofar as is known, with any of the known prior art.

The use of the dual functional additive of the present invention in the manner described above creates an SMC which exhibits superior viscosity index, as well as improved dynamic impact properties, hiφ tarperature retention properties, and pig entability over any in the known prior art.

The following examples are given by way of reference only, and are not intended in any way to be a limitation on the scope or spirit of the present invention.

Examples 1 throuφ 6

Examples 1 through 6 are given to show the method for preparing the prepolymer contemplated by the present invention from either a polyether or a polyester base.

The polyol, either a polyether polyol or a polyester polyol, is dissolved in styrene until a clear, homogenous solution is obtained. The isocyanate is in a reaction kettle and the polyol solution is added to it at the rate of appoximately 1.67 percent by weiφt per minute. During the addition of the polyol, the reactants are maintained at a temperature of approximately 100 F.

After the addition of the polyol, a catalyst is added to the reaction mass and the reactants are allowed to exotherm for approximately 30 minutes. After the reaction temperature stabilizes, usually within 30 minutes of exotherm, the ccmposition is heated to approximately 155° F and maintained at that temperature for an additional 30 minutes. The completion of the reaction is monitored by measuring the free isocyanate content of the reaction product.

The following examples are given to show the prepolymer formed when using either a polyether polyol or a polyester polyol:

Evample 1; Prepolymer;

NSQ = 2 CH 1

Polyether polyol; Eι ^~ = 1000

MDI

75% solids, 25% styrene

Exgpple 2: Prepolymer; m -. z

Oh 1

Polyester polyol; EW = 1000

MDI

75% solids, 25% styrene

Exarple 3: Prepolymer

NCO = 5 CH 1

Polyether polyol; EW = 1000

MDI

75% solids, 25% styrene

Exarpje 4: Prepolymer 2 _ 1_5_ CH 1

Polyether polyol; EW = 1000

MDI

35% solids, 65% styrene

Example 5: Prepolymer

£Ω2 ₌ 1 _* 5. CH 1

Polyester polyol; EW = 1000

35% solids

Example 6: Prepolymer

NQ_ ₌ 1 CH 1

Polyether polyol; EW = 500

MDI

75% solids, 25% styrene

Examples 7 through 9

Examples 7 through 9 are provided to show the i provarents in shrinkage and rooldability which are obtained using the prepolymer blend of the present invention. Exarple 7, containing no prepolymer and no isocyanate, serves as the control, whereas Example 8 depicts the results when using a polyether based isocyanate terminated urethane prepolymer, and Example 9 serves to depict the results expected when using an isocyanate terminated urethane prepolymer based on a polyester polyol. The advantages ejected when using a prepolymer according to the present invention include improved shrinkage properties as well as moldability over the control "paste" blend. In each of the cited examples, the value is defined as I' ^S ^ *^ *«*» ^** \ is the moldability of the paste.

Exarple 7:

Polyester resin 67

Acrylic syrup 33

Urethane prepolymer

Styrene

Free radical catalyst 1

Mold release agent 3

Magnesiur oxide

Magnesiur hydroxide 1

Calcium Carbonate 200

NGO/CH 0

Initial viscosity at 100° F. 29000 cps

B-staged viscosity at R.T. 20 x 10 ⁶ cps

Shrinkage, inch/inch 3.6 x 10~ ³

Expansion inc /inch

Molding characteristics:

Rvalue 0.065

Viscosity niarber 30

Exarple 8:

Polyester resin 67

Acrylic syrup 16.5

Urethane prepolymer (Ex. 1) 7.7

Styrene 8.8

Free radical catalyst 1

Mold release agent 3

Magnesium oxide -

Magnesium hydroxide 1

Calcium carbonate 200

NO0/CH 0.223

Initial viscosity of 100° F. 36800 cps

B-stages viscosity at R.T. 29 x 10 ⁶ . cps

Shrinkage, inch/inch 3.5 x 10" ³

Expansion inc inch -

Molding characteristics:

Rvalue 0.133

Viscosity number 150

Exarple 9:

Polyester resin 67

Acrylic syrup 16.5

Urethane prepolymer (Ex. 2) 7.7

Styrene

Free radical catalyst 1

Mold release agent 3

Magnesium oxide -

Magnesium hydroxide 1

Calcium carbonate 200

NOD/OH 0.223

Initial viscosity at 100° F. 20000 cps B-staged viscosity at R.T. 26 x 10 ⁶ cps Shrinkage, incVinch 8.8 x 10~ ³ Expansion inch/inch Molding characteristic: Rvalue 0.159

Viscosity number 107

Examples 10 through 13 Examples 10 throuφ 13 are provided to depict the effect various specific ratios of isocyanate to hydroxyl groups in polyester and/or polyester resin systems as it relates to shrinkage characteristics and moldability. Example 10 acts as the control, having no isocyanate terminated urethane prepolymer present and a polyester resin based upon polymetbyl methacrylate and styrene and having similar properties as Example 7, namely, poor shrinkage properties and poor moldability.

Example 11 depicts the effects of the isocyante terminated urethane prepolymer product of Example 3 having a styrene blend and an NOO/CH ratio of 5:1 on a polyester resin product. The prepolymer according to Example 11 shews a sliφtly hiφer shrinkage than the control of Example 10, but still within normally acceptable parameters. Further, Example 11 depicts an improved moldability relative to the control of Exarple 10.

Example 12 depicts the effect of an isocyanate terminated urethane prepolymer based on a polyether polyol formed from a styrene blend having an NCD/CH ratio of 1.5/1. Bie example is provided to show the effect of different ratios of NOO/CH relative to shrinkage and moldability, which in this example are much improved over the control of Example 10.

Example 13 is provided to shew the results to be expected relative to shrinkage and moldability when using an isocyanate terminated

urethane prepolymer based on a polyester polyol in a styrene blend which forms the polyester resin of the Exarple. As seen in Example 13, an NGO/OH of 1.5/1 is used in the polyester based prepolymer resulting in a hiφer shrinkage than the control of Example 10, but still within normally acceptable parameters, as well as improved moldability over that exhibited by the control of Example 10.

Exarple 10:

Polyester resin 70

Acrylic syrup 30 Urethane prepolymer Styrene

Free radical catalyst 1 Mold release agent

Magnesium oxide 0.6 Magnesium hydroxide

Calcium carbonate 200

NGO/OH 0

Initial viscosity at 100° F. 28000 cps

Br-staged viscosity at R.T. 20 x 10 ⁶ cps

Shrinkage, inch/inch 4 x 10~^ Expansion inch/inch Molding characteristics:

Rvalue 0.067

Viscosity number 335

.ExarøLfi-ll:

Polyester resin 70

Acrylic syrup

Urethane prepolymer (Ex. 3) 13.5

Styrene 16

Free radical catalyst 1

Mold release agent 3

Magnesium oxide 0.6 Magnesium hydroxide Calciur carbonate 200 NOO/CH 0.761

Initial viscosity at 100°E 34000 cps B-staged viscosity at R.T. 40 x 10 ⁶ cps Shrinkage, inch/inch 6.0 x 10" ³ Expansion ___nch/inch Molding characteristics: 2* value 0.229 Viscosity number 58.3 Exarple 12: Polyester resin 70 Acrylic syrup

Urethane prepolymer (Ex. 4) 30 Styrene

Free radical catalyst 1 Mold release agent 3 Magnesium oxide 0.6 Magnesiur hydroxide Calciur carbonate 200 NOO/CH 0.134

Initial viscosity at 100° F. 104000 cps B--staged viscosity at R.T. 65 x 10 ⁶ cps Shrinkage, inch/inch 2.1 x 10" ³ Expansion inct inch Molding characteristic: value 0.226

Viscosity number 45.3 Exarple 13; Polyester resin 70

Acrylic syrup

Urethane prepolymer (Ex. 5) 30

Styrene

Free radical catalyst 1

Mold release agent 3

Magnesium oxide 0.6

Magnesium hydroxide

Calciur carbonate 200

NGO/CH 0.134

Initial viscosity at 100 °F. 31200 cps

B-staged viscosity at R.T. 60 x 10 ⁶ cps

Shrinkage, inclV'inch 7.8 x 10- ³

Expansion inch/inch

Molding characteristic: Rvalue 0.571

Viscosity number 11.1

Examples 14 and 15 Examples 14 and 15 are provided to depict the shrinkage characteristics of the prepolymer of the present invention contrasting the shrinkages observed when using a polyether polyol having the equivalent weiφt (E.W.) of 1000 and 500, which corresponds to the polyols cαrmonly kncwn as BASF PzOlO and BASF P1010, respectively. In both examples, the NGO/CH is 2/1, which is within the preferred ranges of the present invention.

Exarple 14:

Polyester resin 50

Acrylic syrup 27.8

Urethane prepolymer (Ex. 1) 11.75

Styrene 8.4

Polyether polyol 2.9

Free radical catalyst 1

Mold release agent 3

Magnesium oxide -

Magnesium hydroxide 2

Calciur carbonate 219

NGO/CH 0.272

Initial viscosity at 100° F. 56000 cps

B-staged viscosity at R.T. 30 x 10 ⁶ cps

Shrinkage, inch/inch -

Expansion inch/inch 2.5 x lO- ³

Molding characteristic: value -

Viscosity number -

Example 15:

Polyester resin 50

Acrylic syrup 27.8

Urethane prepolymer (Ex. 6) 11.75

Styrene 8.4

Polyether polyol 2.9

Free radical catalyst 1

Mold release agent 3

Magnesium oxide -

Magnesium hydroxide 2

Calciur carbonate 219

NGO/CH 0.466

Initial viscosity at 100° F. 51200 cps

B-staged viscosity at R.T. 51 x 10 ⁶ cps

Shrinkage, inch/inch 0.4 x lO- ³

Expansion inch/inch -

Molding characteristic: value -

Viscosity number —

Examples 16 and 17

Examples 16 and 17 are provided to contrast the dynamic impact characteristics of conventional prior art SMCs with the SMC formed by the present invention.

Exarple 16:

Polyester resin 57

Acrylic syrup 43

Urethane prepolymer -

Styrene -

Free radical catalyst 1

Mold release agent 3

Magnesiur oxide -

Magnesiur hydroxide 2

Calciur carbonate 190

1" cut glass raving 115

Elexural strength, (ASTM D-790-70) 26000 psi

Elexural modulus, (ASTM D-790-70) 1.7 x 10 ⁶ psi

Tensile strength, (ASTM D-683-68) 10500 psi

Dynamic impact strength. at initial of radius at 6 mph.

0.120" thickness at 75° F:

Energy absorbed 5.0 ft lbs.

Maximum load 550 lbs.

Exarple 17:

Polyester resin 57

Acrylic syrup 25.1

Urethane prepolymer (Ex. 1) 11.6

Styrene 6.3

Free radical catalyst 1

Mold release agent 3

Magnesiur oxide -

Magnesiur hydroxide 2 Calciur carbonate 190 1" cut glass raving 115 Flexural strength, (ASTM D-790-70) 26000 psi Flexural modulus, (ASTM D-790-70) 1.75 x 10 ⁶ psi Tensile strength, (ASTM E--683- 8) 10500 psi lynamic impact strength, at initial of radius at 6 mph, 0.120" thickness at 75° F: Energy absorbed 7.8 ft lbs. Maximum load 800 lbs.

It will be readily understood that various modifications may be made by those learned in the art without departing frαr the scope or spirit of the present invention.