BALLISTIC MATERIALS

Abstract: The present invention provides a fiberglass composite which possesses outstanding armor properties. This ballistic resistant composite material employs a high strength magnesia aluminosilicate glass fabric and a prescribed phenol for­ maldehyde condensation product as the matrix resin. The composite is produced from a prepeg by molding under con­ trolled conditions and the prepeg material is formed with a controlled heating cycle.

Description: The present invention relates to glass fiber composite articles and more particularly it relates to fiberglass composite articles which have ballistic resistant properties. Even yet more particularly the present invention relates to the formation of thick, self-supportable ballistic resistant fiber composites which may be employed as liners or as structural armor. Ballistic resistant articles which contain high strength fibers for use as structural members and panels for a wide variety of military equipment are known. Thus far one of the more successful fibers is a polyaramide and more specifically poly (phenylenediamine terephthalamide). Such fibers, in fabric form, are in their usual method of use encapsulated or embedded in a composite article of a thermoset resin. In order for a composite to have its broadest application for a wide variety of ballistic resistant applications, it is important that it likewise possess a wide balance of important properties. Such uses range from structural armor to spall suppression liners. The properties include, of course, proper ballistic performance, that is, the composite functions satisfactorily as a ballistic armor system. Other required qualities are that the material be stiff and self-supporting, machineable, able to be formed into thick durable sections, fire-resistant, smoke-resistant, non-toxic, non-conductive and thermally insulative. One important property is that the composite be capable of being easily cut, trimmed, and drilled with if need be carbide or diamond tips. Composites with this needed balance of properties are not easily manufactured or widely available. A currently used laminate, or composite, employs a polyaramide and a laminating resin which is the cured reaction product of a polyvinyl butyral, phenol formaldehyde, trimethylol phenol, and phthalic anhydride. Such laminates have utility for armor applications and spall liners but one of their more notable deficiencies is that they are not easily machined and can be easily damaged (scratched etc.). Such laminates, for a given weight per square foot, generally are quite thick, and bulky, and yet are highly susceptible to buckling and high deformations. These characteristics lead to a waste of highly valuable space in military applications. Thus it will be seen that there is a need in the art for providing composites with a balance of properties to make them useful for a wide variety of structural armor applications and spall liners and which are made of materials other than a polyaramide. There is also a need to provide for ballistic resistant composite materials which can be more easily machined and which have good water and weather resistant properties. It will also be apparent that there is a need for composites which on a weight basis have increased ballistic performance characteristics; that is there is a need for materials have increased ballistic performance (V₅₀ PBL) at a given areal density. Such type materials with these many needed properties are reliably made in accordance with this invention and which for a given weight per unit of area are not bulky and have good resistance to buckling and deformation. In GB-A-2173810 there is described a procedure for producing molded articles by preparing a resole resin by heating non-aqueous phenol with paraformaldehyde in the presence of an alkaline catalyst; cooling the resulting aqueous solution of phenol-formaldehyde condensation product to room temperature to arrest condensation while the condensation product is liquid; mixing the aqueous solution with glass fibers, possibly in the form of a web, and a curing agent; heating the mixture to 80 to 120°C (to effect further condensation and to evaporate water) for such a period that on cooling to 20°C the viscosity of the mixture is such that the phenolic resin does not drain from the fibers; and forming the article by heating under pressure in a mold. That document, however, makes no reference or suggestion that such a procedure is in any way applicable to the manufacture of specialised products such as ballistic-resistant materials by suitable selection of individual ingredients and particular processing parameters. In accordance with the present invention, ballistic-resistant materials are provided which are fire-resistant, smoke-resistant, non-toxic, non-conductive, self-supporting and stiff, machineable, thick and strong so as to allow their use in structural armor applications and as ballistic resistant liners. An important feature of these composites is that they are of high uniform quality, and even thick sections do not suffer from the presence of entrapped by-product water. Such composites can be formed by a process wherein a easily handleable prepeg is first formed. This prepreg is formed by coating, or impregnating, a balanced symmetric fabric of interlaced high strength magnesia aluminosilicate glass fibers with a solution of a partially condensed, further condensable low molecular weight phenol formaldehyde resole reaction product and evaporating the solvent from the solution. The coated, or impregnated, fabric is then heated, but not substantially higher than its gel point, to increase the resole molecular weight and thereby form the easily handleable prepeg. Prepeg plies are then molded by heating, first of all, to a temperature not substantially higher than the gel point of the resin and under contact pressure and holding it at that temperature under such contact pressure to allow by-product water to gradually escape; they are then heated to an elevated temperature and held at that temperature to fully polycondense and cure the resin. A plurality plies of such prepegs will be molded and thereby form composites having an areas density greater than at least about 12.2 Kg per square meter (2.5 pounds per square foot). Typically the laminated composite panels formed in accordance with the present invention, when formed to a thickness of the order of about 12.7 mm (1/2 inch) with an areal density between about 22.0 Kg per square meter (4.5 pounds per square foot) to about 25.4 Kg per square meter (5.2 pounds per square foot), will have a V₅₀ value (protection ballistic limit) of in excess of about 827.5 meters per second (2,715 feet per second) up to as high as 873 meters per second (2,865 feet per second) or even higher with (2.6 gram steel 7.62 mm fragment simulating projectiles). These values are significantly higher than those reported in U.S. Patent 4,664,967. In practicing the present invention conventional equipment and techniques may be employed both for producing the prepreg and for the compression molding of the prepregs into the final composite product. Thus, for example, when forming the prepreg, a fabric of interlaced high strength magnesia aluminosilicate glass fibers can be dipped into a solution of the phenol formaldehyde resin, passed through nip rolls, the solvent evaporated and a controlled further condensation heat treatment given to form a handleable prepreg. Compression molding of a plurality of plies of the prepreg material can be done using any commercially available compression molding equipment. The number of prepreg plies which are compression molded will generally be sufficient to form a final composite product having an areal density of at least about 12.2 Kg per square meter (2.5 pounds per square foot). For other applications, for example, ship board type applications it generally will be desirable to form composites having densities in excess of about 36.6 Kg per square meter (7.5 pounds per square foot) and typically between about 36.6 Kg/M² (7.5 pounds per square foot) to about 41.5 Kg/M² (8.5 pounds per square foot). Satisfactory vehicle spall liners are produced by using a sufficient number of plies to produce areal density of an excess of about 19 Kg/M² (3.9 pounds per square foot) and typically between about 19 Kg/M² (3.9 pounds per square foot) and about 25.4 Kg per square meter (5.2 pounds per square foot). Usually on the order of about 13 to about 26 plies will produce outstanding products. Typically, with a glass content in the final product on the order of about 78% to about 84% (by weight), outstanding composites are achieved. Generally the ballistic resistant panels of this invention will have a thickness on the order of at least about 6.4 millimeter (1/4 inch) and may be as thick as 76.2 mm (3 inches) or more. The flexural strengths of the final ballistic resistant composites of the present invention typically will be in excess of about 172,369 kilopascals (25,000 psi) and the flexural modulus will generally be on the order of an excess of about 27.6 x 10⁶ kilopascals (4,000,000 psi). As indicated, a balanced symmetric fabric of interlaced high strength magnesia aluminosilicate glass fibers is employed. By balanced symmetric fabric of interlaced fibers is meant a fabirc comprised of an assembly of approximately parallel and perpendicular equal spaced, equal weight glass fibers. Preferred fabrics are those with biaxial symmetry. Thus, for example, a (plus and minus 45) helical filament-wound glass mat can be employed as well as a stitched glass fiber assembly, but it is most preferred that a woven glass roving be used. The woven roving may be of a plain weave or a twill weave (for example 1:3), or satin weave or modifications thereof allwing a balanced symmetric structure. The weight per unit area of the fabric employed preferably will be between at least about 18 to about 48 oz/yd² (610 to 1627 g/m²) with a fabirc having a value of about 813 grams per square meter (24 ounces per square yard) producing outstanding results. The interlaced fibers of the glass fabric generally will have a yield of less than about 1510 meters/kilogram (750 yards per pound). Fibers with yields on the order of about 504 meters/kilograms (250 yards per pound) produce good quality materials. Generally it is preferred to employ fibers with a yield in excess of about 201 meters per kilogram (100 yards per pound). Monofilament fibers which form the fabric, or roving, and which are of G or K diameter produce highly desirable results. These monofilament fibers have diameters of about 15 microns or less and generally about 8 to about 15 microns. Magnesia aluminosilicate glass fibers used herein are high strength fibers and typically have a tensile strength in excess of about 3.5 x 10⁶ kilopascals (500,000 psi). These fibers are roughly about two-thirds by weight silica, and typically on the order of about 65% by weight silica, and one-third being magnesia and alumina with the alumina being present in a greater amount than the magnesia. Typically alumina will be about 25% by weight and magnesia about 10% by weight for outstanding results. Best results are obtained when the fibers have a water resistant, impact debondable size coating thereon. Preferred size coatings are sizes containing an epoxy based film former and an epoxy silane coupling agent along with other conventional materials. Water resistance of the size can be tested by a boiling water test in which fiber composites are immersed for about 2 hours and then dried. Fibers which retain at least about 80% of their original flexural strength possess sufficient water resistance. (See ASTM-D570 and ASTM-D790 for fuller details). By impact debondable size is meant a size which, during processing, when glass fiber bundles are placed in the liquid matrix resin allows the glass fibers to disperse well but, when within the composite matrix, the sized fibers have an interfacial shear strength, or adhesion, with the resin matrix to permit filament and bundle debonding and pullout which balances compressive - shear failure. The latter features can be evaluated by ASTM-D344 (interfacial shear strengths measured by short beam shear test) and ASTM-D695 (a compression test through composite thickness). Interfacial shear strengths by the short beam test of less than 41,369 kilopascals (6,000 psi) are desirable with good results being obtained at about 13,790 kilopascals (2,000 psi). The compression test values are desirably in excess of about 620,528 kilopascals (90,000 psi), preferably in excess of about 689,476 kilopascals (100,000 psi) with values in the approximate range of 689,476-827-371 kilopascals (100,000-120,000 psi) producing good results. The phenol formaldehyde resin is a resole phenolic and is not new per se. These types of resins have been used in the past for forming phenolic resin-fiber composites by such conventional techniques as hand lay up, hot molding, vacuum injection, filament winding, pultrusion or prepreg techniques. Satisfactory results will be obtained by employing results in which the molar reactant ratio of formaldehyde to phenol is between about 1:1 to about 3:1, preferably about 1:1 and about 2:1 with best results being obtained at about 1.1:1 to about 1.5 or 1.6:1. Above the 3:1 ratio ballistic resistance or stopping power may be satisfactory but the damage area upon ballistic impact is increased. The damage are includes both the composite deformation and localized delamination or ply separation. These resins are low molecular weight materials and outstanding results have been obtained using resins having weight average molecular weights in the range of about 200 to about 800. The resins are commercially available and are supplied in solvent solutions. Best results have been obtained employing solvent solutions of the partially condensed further condensable low molecular weight phenol formaldehyde resole in which the solutions contain free phenol as well as free formaldehyde. The solutions also can contain free water. Typical solvents employed are ethyl alcohol, isopropyl alcohol and methylethyl ketone or combinations thereof. Best results have been obtained employing solvent solutions containing on the order of about 50 to 70% by weight solids, about 2 or 3% up to about 16 or 17% by weight of free phenol and between about 0.1 up to about 2% by weight of free formaldehyde. Outstanding results were obtained using solids contents between about 60 to 66% by weight, free formaldehyde of about 1% by weight and free phenol between about 5 to about 16% by weight. The solutions which produce best results contain on the order of 24 or 25% of either ethyl alcohol or isopropyl alcohol, with the latter being preferred, and free water being less than about 10%. The viscosities of solutions typically employed for forming the prepreg will be on the order of about 100 to about 400 centipoise. Once the fabric of the interlaced glass fibers is impregnated or coated with the resole phenol solution and the solvent evaporated, the material will be heated to a temperature not substantially higher than the gel point of the resin and held at that temperature for a sufficient period of time to increase its molecular weight and form a prepreg which, upon cooling to room temperature, is easily handleable. It will, of course, be apparent to those skilled in the art that handleability takes in a wide variety of important properties including proper drape, appropriate tack, and good machinability. As used herein the gel point means that stage at which the resole phenolic resin exhibits a rather sudden and somewhat dramatic increase in the viscosity, and generally the rate at which the viscosity increases with time and/or temperature. The gel points are generally between about 135°C (275°F) to about 143°F (290°F). The resole phenol, after this heating, will have an increased molecular weight but still generally less than about 1,500, thus indicating the presence of significant amount of oligomers. If heating is not done for a sufficient period of time, a handleable prepreg will not be formed. Typically it will be too tacky and very difficult to transfer. Excessive heating causes too much polycondensation at this time and, this in turn, will cause difficulties in consolidation during molding. Prior to the above noted staging by heating the resin, the partially condensed further condensable resole has a heat of reaction of about 100 to about 250 Joules per gram. Sufficient heating will generally result in a resin having a decreased heat of reaction, e.g., sufficient to produce a further condensable resin having a heat of reaction of about 10 to about 90 Joules/gram. Alternatively, it may be stated that once the solvent is evaporated, the resole resin material is heated for sufficient period of time such that the solids level is increased and retained in the range of about 64 to about 72%. If desired, and as will be apparent to those skilled in the art various adjuvants, catalyst or other materials can be added to the solvent solution to beneficially impact upon the characteristic features of the final product or to enhance the rate at which they can be formed. Thus, for example, if desired acids like Lewis acids can be added to enhance the rate of curing. Boric acid and para -toluene sulfonic acid are especially desirable. Carbon black can be added for a variety of purposes. In addition to aiding general flow characteristics of the phenolic, carbon black at low levels, for example, 1 to 2% by weight is desirable for coloration purposes. Between 1 and 5% by weight, carbon black will also provide UV protection and higher percentages, up to about 15% by weight, increases the electrical conductivity and the heat of ablation of the ballistic resistant composite. Most desirably the carbon black, if employed, will be employed in the amount of about 2 to 7% by weight and the particle size will be on the order of about 30 to 70 millimicrons. After cooling the prepreg material to room temperature the prepregs may be stored or, if desired, can be immediately used to form the final product. The final product is obtained by stacking a plurality of the prepregs in a compression mold and then controllably heating under controlled pressure to form a final product which is free of entrapped water vapor. Quite surprisingly by following the present teachings a thick resole composite can be easily formed, for example, one on the order of at least about 6.35 mm (1/4 inch) in thickness and, quite surprisingly, even thicker materials for example, 12.7-76.2 mm (1/2 inch to 3 inches) and even thicker. This can be, quite surprisingly, done without significant problems with entrapped water. In contrast if prior art compression molding techniques were followed it would not be possible to make such thick articles. Prior art techniques generally involve heating the material and "bumping" at about 166-177°C (330 to 350°F). In such prior art techniques the mold is closed, pressurized and heated to about 166°C (330°F) the "bumped" by opening the mold, followed by an optional repeating of the cycle, then final molding. These bumping cycles of the prior art are not adequate to properly release the moisture by-product when forming thick composites. In accordance with the present invention, the prepregs are heated to a temperature not substantially higher than the gel point while under contact pressure of the compression mold and it is held at that temperature and pressure to consolidate and allow volatile condensation products to escape. Contact pressure essentially means the pressure inherently applied by the mold tools without positive and affirmative pressurization. With a relatively large compression molding machine this contact pressure may be on the order of about 207 kilopascals (30 psi) or less (with smaller molding units the contact pressure will be on the order of about 13.8 to 20.6 kilopascals (2 to 3 pounds per square inch)). After heating under this contact pressure, the mold pressure is then increased and the temperature taken up to a curing temperature, for example, 149 to 177°C (340 to 350°F). The material is then held there for a sufficient period of time to fully poly condense and cure the phenol-formaldehyde reaction product into a crosslinked structure, whereby forming ballistic resistant panels (including rectilinear and curvilinear shapes) having the properties indicated above. An exemplary heating cycle would be to heat the stacked plies of the prepreg under contact pressure up to 135°C (275°F) and hold it there for approximately 7 minutes after which time the pressure can be increased and the temperature taken to about 171 to 177°C (340 to 350°F). The materials are then held at that temperature for on the order of about 30 minutes and generally under a pressure of at least about 793 kilopascals (115 psi) and typically in the range of about 793 kilopascals (115 psi) to 2,068 kilopascals (300 psi). After this, the material is cooled under pressure to about 65.6°C (150°F) after which time the pressure is released and the final material cooled to room temperature. As generally indicated above, the areal density of the final products will be at least about 12.2 kilograms per square meter (2.5 pounds per square foot) and more desirably at least about 19.5 kilograms per square meter (4 pounds per square foot). This areal density, of course, is obtained by varying the number of plies that are employed in compression molding the final product. While the above enables those skilled in the art to make and use the present invention, a more specific example follows. EXAMPLE Woven roving available from Owens-Corning Fiberglas Corporation under the designation S-2 Glass, 250 AA463 5X5.12 PW (a plain weave woven roving of sized magnesia aluminosilicate glass fibers of G filament diameter) and generally of the following specifications: an S-2 Glass input roving yield of 504 meters per kilogram (250 yards per pound), a woven weight of 813 grams per square meter (24 ounces per square yard) with a plain weave construction of 1.9 warp ends per centimeter (5 warp ends per inch) and 2.0 fill ends per centimeter (5.12 fill ends per inch) was employed. The resole Phenolic solution was that commercially available from the Borden Chemical Company as their designation SC1008. This is a solution containing about 60 to about 66% by weight solids and on the order of about 25% by weight isopropyl alcohol as the solvent. Free formaldehyde is about 1% and free phenol about 10 to 16% by weight. It had a pH of about 8.0 and a viscosity of about 180 to 300 centipoise. The SC-1008 resin was applied and transferred to the woven roving by compaction rollers with a nip setting of 22-26 mils. (Alternatively a doctor blade technique can be used.) The solvent was evaporated and the impregnated woven roving was heated to, and held at a temperature of about 121-135°C (250° to 275°F) for about 10-12 minutes. The heat of reaction of the phenol formaldehyde was about 40 Joules per gram at 68% solids. After cooling the prepregs were compression molded using conventional peel ply materials. The tools of the compression mold can also be treated with a release material to minimize sticking. Twenty-six plies of prepreg were positioned in a preheated mold, the plies being sufficient to provide a final product thickness of about 12.7 millimeter (one-half inch). The compression mold was closed but no affirmative pressure was added to the mold and only the contact pressure of the mold tools contributed to the pressure. This was on the order of about 34.5 kilopascals (5 pounds per square inch). The mold was at a temperature of about 135°C (275°F) and the prepreg plies were held at that temperature for about 7 minutes. A thermocouple was employed to determine heat transfer and be certain that essentially the entire mass of prepreg had reached that 135°C (275°F) temperature in the 7 minute interval. After that dwell time the mold was pressurized (anywhere between 793 kilopascals to 2,068 kilopascals (115 psi to 300 psi)) and heated to 171-177°C (340°-350°F). It took about 15 minutes to reach that temperature and then the prepreg materials were held at that temperature for approximately 30 minutes. Over about a 10 minute interval the molded prepregs were then cooled, under pressure, to about 65.6°C (150°F), the pressure then released and the molded prepreg cooled to room temperature. The material produced was fire-resistant, smoke resistant and essentially non-toxic when burned. The laminate was stiff and self-supporting and was easily machined using a diamond tip and carbide water cooled tools and virtually free of entrapped water. The thickness of laminates was about 12.7 millimeters (1/2 inch) and laminates had an areal density of about 22 kilograms per square meter (4.5 pounds per square foot) to about 25.4 kilograms per square meter (5.2 pounds per square foot) and V₅₀ values 2.6 gram (44 grain) steel 7.62 millimeter (0.30 caliber) fragment simulating projectiles of between about 827.5 meters per second (2,715 feet per second) to about 873 meters per second (2,865 feet per second). These are outstanding values, especially for spall liners. In contrast, and in comparative testing, when the prior art technique was employed of simply heating the compression mold to about 166 to 177°C (330 to 350°F) and then bumping by opening the molds to release water vapor and then closing and continuing the curing, problems with forming a quality product existed. That is thick, high areal density materials could not be formed because of the inability to release the by-product water at thicknesses of greater than about 6.35 mm (1/4 inch). With such prior art technique such composites have unacceptable ballistic performance levels. The present invention describes a fiber glass composite of a high strength magnesia aluminosilicate glass fabric and a phenol formaldehyde condensation product as the matrix resin. The composite has a high resistance to penetration by ballistic penetrants and can be used for armor or as a spall liner for military vehicles.

Claims: 1. A glass fiber composite which is resistant to buckling and deformation, fire- and smoke-resistant, machineable and self-supporting, comprising a plurality of layers of a balanced interlaced high strength magnesia aluminosilicate glass fiber fabric in a matrix of a cured phenol formaldehyde resole resin, the composite having an areal density of at least 12. 2 kilograms per square meter (2.5 pounds per square foot) and being substantially free of entrapped water vapor. 2. A composite according to claim 1 having an areal density of at least 19.5 kilograms per square meter (4 pounds per square foot). 3. A composite according to claim 1 or claim 2 having a flexural strength in excess of 172,369 kilopascals (25,000 psi) and a flexural modulus in excess of 27.6 x 10⁶ kilopascals (4,000,000 psi). 4. A composite according to claim 3 having an areal density from 2 2 to 2 5. 4 kilograms per square meter (4.5 to 5. 2 pounds per square foot) and a V₅₀ value from 827.5 to 873 meters per second (2,715 to 2,865 feet per second). 5. A composite according to any one of claims 1 to 4, wherein the fabric is a plain weave or twill weave roving. 6. A composite according to any one of claims 1 to 5, wherein the fibers have a tensile strength of at least 3.5 x 10⁶ kilopascals (500,000 psi). 7. A composite according to any one of claims 1 to 6, wherein the fibers have an interfacial shear strength with respect to the phenol formaldehyde resole of less than 41,369 kilopascals (6,000 psi). 8. A composite according to any one of claims 1 to 7, containing 78 to 84% by weight of glass. 9. A composite according to any one of claims 1 to 8, wherein the fibers have a filament diameter of 8 to 15 µm and have a yield of about 504 meters per kilogram (250 yards per pound). 10. A process for producing a self-supporting, machineable, fire-, smoke- and ballistic-resistant composite material according to any one of claims 1 to 9, comprising the steps of: coating a balanced symmetric fabric of interlaced high strength magnesia aluminosilicate glass fibers with a solution of a partially condensed further condensable phenol formaldehyde resole reaction product, formed by reacting formaldehyde and phenol in a molar ratio between 1:1 and 3:1, the solution containing free phenol and free formaldehyde, the fibers bearing a water-resistant debondable size coating and having a yield of less than about 1510 meters per kilogram (750 yards per pound); evaporating solvent from the solution, heating the resole-coated fabric to a temperature up to the gel point of the phenol formaldehyde resole reaction product to further condense the resole and inc:ease its molecular weight and cooling the reaction product to form a handleable prepreg; stacking a plurality of prepregs into a compression mold; heating the prepregs under contact pressure in the mold to a temperature up to the gel point of the phenol formaldehyde reaction product and allowing volatile condensation by-products to escape; and further heating the prepregs to a temperature of at least 171°C (340°F) under a pressure higher than the contact pressure, to substantially fully polycondense and cure the phenol formaldehyde reaction product and form a ballistic resistant composite material. 11. A process according to claim 10, wherein the glass fiber fabric has a unit area weight from 610 to 1627 grams per square meter (18 to 48 ounces per square yard). 12. A process according to claim 10 or claim 11, wherein the phenol formaldehyde resole resin is forced by reacting formaldehvde and phenol in a molar ratio of 1.1:1 to 1.6:1. 13. A process according to any one of claims 10 to 12, wherein the phenol formaldehyde resole in the solution has a weight average molecular weight from 200 to 800. 14. A process according to any one of claims 10 to 13, wherein the coated fabric is heated below the gel point to increase the molecular weight of the resole to 1,500 or less. 15. A process according to any one of claims 10 to 14, wherein the gel point is 135 to 143°C (275 to 290°F). 16. A process according to any one of claims 10 to 15, after heating the resole has a heat of reaction of 10 to 90 Joules per gram. 17. A process according to any one of claims 10 to 16, wherein the contact pressure is 207 kilopascals (30 psi) or less. 18. A process according to claim 17, wherein the contact pressure is 20.7 to 138 kilopascals (3 to 20 psi) and wherein the stacked prepregs are maintained under contact pressure at about 135°C (275°F) for at least 7 minutes. 19. A process according to any one of claims 10 to 18, wherein prepregs are maintained under a mold pressure of at least 793 kilopascals (115 psi) to cure the phenol formaldehyde reaction product. 20. A process according to any one of claims 10 to 19, wherein the solution of phenol formaldehyde resole reaction product contains carbon black.

Inventors: HARTMAN, DAVID, RANDALL
Applicants: OWENS-CORNING FIBERGLAS CORPORATION
Application year: 1988
Main classification: F41H5
IPC codes: F41H5, B29C43, C03C25, B29K61, C08J5, B29K105