FLEXIBLE MULTIPLY TOWPREG, PRODUCTS THEREFROM AND METHOD OF PRODUCTION THEREFOR

Abstract: This invention relates to an improved flexible multiply towpreg, products therefrom, and methods of production therefor. The improved flexible towpreg comprises a plurality of towpreg plies (134) which comprise reinforcing filaments (132) and matrix forming material (131); the reinforcing filaments being substantially wet out by the matrix forming material such that the towpreg plies are substantially void-free composite articles, and the towpreg plies having an average thickness less than about 100 microns.

Description: FLEXIBLE MULTIPLY TOWPREG, PRODUCTS THEREFROM AND METHOD OF PRODUCTION THEREFOR BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention is directed to flexible multiply towpreg, products therefrom, and a method of production therefor and, more specifically, a very flexible multiply towpreg suitable for weaving, braiding, and the like, products made therefrom, and a method for producing such a towpreg. The flexible multiply towpreg can be formed into a flexible multiply towpreg tape of uniform dimensions and accurate geometry suitable for filament winding, pultrusion, and the like; a non-woven towpreg fabric suitable for further processing to form multi-dimensional fabrics, preforms, and composite structures; and towpregs comprising continuous fibers or filaments combined with a matrix resin comprising, in part, recycled plastics. 2. Discussion of the Prior Art Towpregs comprising fibers or filaments combined with a matrix resin are known in the art and typically are called "prepregs"; thus, towpregs are one form of prepreg. Conventional prepreg consists of hundreds or thousands of fibers or filaments embedded in a continuous mass of matrix. The reinforcing fibers typically used are available commercially in continuous form in "bundles" of filaments known as "tows", which vary widely in number of filaments per tow. Many matrix resins are available, however two kinds of matrix resin systems dominate the prior art: thermoplastic and partially cured thermoset polymers. Thermoplastic polymers have been used widely as matrices for towpregs and other composites, and potentially are useful as matrices for advanced composites for aerospace applications, among others. Thermoplastics have advantages over thermosetting materials in fracture toughness, impact strength and environmental resistance. Thermoplastics also provide prepregs with indefinite shelf life, give the fabricator better quality assurance and avoid the storage and refrigeration problems associated with thermosetting prepregs. Thermoplastic molecules can be tougher than the rigid cross-linked network of many thermosets; few of the toughened thermosets have met the combined requirements of damage tolerance and hot/wet compression strength necessary for use in aerospace composites. The disadvantage of thermoplastic polymers as a composite matrix material is the difficulty of uniformly coating the fibers due to the high viscosity of the molten polymer. Thermoplastic prepreg typically is rigid and is not well-suited for weaving, braiding or laying up preforms, as the resulting fabrics are stiff. Similarly, the rigidity of thermoplastic coated prepreg complicates the filament winding and formation of complex shapes; heat must be focused at the point of contact to achieve conformability during layup. Thermoset polymers also are used as matrix material for prepregs. Prepreg that contain thermosetting prepolymers, although relatively flexible, usually are tacky, and thus require a protective release coating which must be removed prior to use. While thermoset prepreg is acceptable for certain applications, such as filament winding, its tackiness and the requirement of a protective release coating make thermoset prepreg unfeasible for weaving, braiding, or the production of chopped fiber feed stock for bulk or sheet molding compounds. Two other types of towpreg are metal matrix towpreg, which is similar to thermoplastic towpreg, and partially cured ceramic towpreg, which is similar to thermoset towpreg. However, due to the limited markets for metal and ceramic composites, these materials generally are not available and have not been the focus of developments in manufacturing technology. Metal and ceramic matrix towpregs can be manufactured in a manner and form analogous to thermoplastic and thermosetting towpregs. Continuous fiber prepregs can be produced by a number of impregnation methods including hot melt, solution, emulsion, slurry, surface polymerization, fiber commingling, film interleaving, electroplating, and dry powder techniques. In hot melt processing, impregnation may be accomplished by forcing the fiber and resin through a die at high temperature under conditions that create high shear rates. Due to the high temperatures of this process, the thermoplastic material can degrade. Other disadvantages of this process include the high stress applied to the tow and difficulties in impregnating the fiber tows with thermoplastics. In solution coating, the matrix material is dissolved in solvent and the tow is passed through this solution and then dried to evaporate the solvent. Two disadvantages associated with this process are that thermoplastics usually exhibit limited solubility at high concentration, and most engineering thermoplastics cannot be dissolved in a low boiling-point solvent at room temperature. Additionally, high solution viscosity results in the same impregnation problems as with hot melt, as well as causing the fibers to stick together. Another problem is the difficulty in removing the solvent. Further, traces of solvent left in the prepreg lead to undesirable porosity in the composite. An emulsion process is one way to apply powdered matrix material with a very small particle size to fiber tow by synthesizing the resin as an aqueous emulsion with a surfactant. The problem with this process is that the removal of the surfactant from the final towpreg is difficult. Slurry coating or wet powder processing is a non-solvent coating technique designed to resolve the problem of the insolubility of most thermoplastics in a solvent at room temperature. In slurry coating, the powder is suspended in a liquid medium, generally water, wherein no solvency exists between the resin and the medium, and the fiber bundles are drawn through the slurry. The particulate matrix slurry does not wetout the fiber, resulting in the need for higher pressures to consolidate the matrix and fibers into a composite. This prepreg can be tacky and therefore is not suitable for weaving or braiding. Other disadvantages include the necessity for the removal of the liquid medium, volatiles, and dispersants or surfactants, which are used to form the polymer/liquid colloidal state, the likelihood of aggregates in the slurry caused by poor mixing, and the possibility that polymer particles will settle during processing. To achieve intimate mixing in emulsion or slurry coating, the particle size of the slurry or emulsion should be smaller than the fiber diameter. For many of the thermoplastics that cannot be made by emulsion or dispersion polymerization, it is extremely difficult to produce such fine powder. Thus, a coarse blend between fibers and particles is obtained. The quality of the blend decreases as the particle size increases, leading to poor matrix distribution in the consolidated composite and poor composite performance. In surface polymerization, coating results from the polymerization of the polymer matrix on the fiber substrate. Disadvantages associated with this process include the need to remove undesired materials, such as solvents, inhibitors, or by-products of the polymerization reactions. Surface polymerization only can be conducted by special techniques, such as electropolymerization, which cannot be used to produce many of the polymeric matrices of commercial interest. In fiber commingling, the polymeric matrix is introduced in fibrous form. Polymeric and reinforcing fibers are mingled as dry blends; however, wetting of the fiber by a process such as melting the polymer fiber is deferred until the composite is consolidated. Effective impregnation depends on the degree of randomness of the intermingling of the resin and fiber throughout the system. As no wetting of the reinforcing fibers by the matrix material occurs in this tow, higher pressures are needed to consolidate the towpreg under equivalent processing times and temperatures into a composite, as compared to completely wetted towpreg. Film casting is one method for producing prepreg that resolves some of the problems associated with hot melt impregnation of thermoplastics. It consists of stacking a film layer of matrix material cast from either hot melt or solution over the towpreg fibers. The fibers sandwiched between two films are heated and calendered to force the resin into the fibers. A flexible metal matrix towpreg has been produced by electroplating by American Cyanamid. Each fiber is completely wet-out and uniformly coated with the metal matrix. This towpreg has desirable properties for weaving, braiding, filament winding, or for conversion to bulk or sheet molding compound feedstocks. Additionally, this towpreg does not require high pressure for consolidation. However, electroplating has a disadvantage in that systems that can «e adapted to electroplating are limited. Most ceramic and polymeric matrices of commercial interest cannot be electroplated on reinforcing fibers. As the filaments or fibers comprise one of the electrodes, the reinforcing fiber must be conductive and fibers, such as glass fibers and organic fibers, cannot be electroplated. Powder coating of tow is the most recent method developed for making prepreg. The significant advantages are that no solvent is required and high stresses are not introduced in the process. The ultimate goal for almost all powder coating applications is the ability to deposit a thin, even thickness, high quality coating as efficiently as possible. The powdered resin also must be solid at ambient and elevated storage temperatures, and be capable of melting to achieve a low viscosity to permit flow and to penetrate the fiber tow when heated. Dry powder coating has many advantages because the elimination of a wet base, solvent or water, facilitates reclamation of the coating material. This is an important economic advantage that promises a potential 100% utilization of powder plus elimination of expensive solvents that are flushed off and inevitably wasted. Thus, powder coating was conceived and has grown largely on these potential benefits. Another method of powder coating fibers with matrix is the ATOCHEM method of impregnating fibers with dry thermoplastic polymer powder and then covering the coated fibers with a thermoplastic sheath. However, as the matrix is not melted onto the fibers, only fibers in contact with the sheath are wetted with the matrix. Consolidating this towpreg also requires higher pressures under comparable processing conditions than completely wetout towpreg. Furthermore, as in slurry coating, a fine polymer powder, generally less than 20 microns, is recommended for this process. Producing such fine powder from thermoplastics can be very expensive. Towpreg must contain sufficient matrix, typically over 25% by volume, to permit consolidation of the components into a substantially void-free composite structure without requiring the incorporation of more matrix material. Linear towpreg can be converted into two and three dimensional product forms by weaving, braiding, filament winding, and other known processes. Alternatively, these towpregs can be used to create a discontinuous fiber reinforced feedstock for molding by chopping, cutting, or like known processes. BRIEF SUMMARY OF THE INVENTION The base towpreg of the present invention is suitable for weaving, braiding, filament winding, and further processing into useful forms as it has a minimum bending radius of no greater than about 15 mm and an average ply thickness that does not exceed about 100 microns. Atthough the ply thickness may be limited by the above requirements to be useful in weaving and braiding, it is not necessary to constrain the size of the towpreg provided the plies comprising the towpreg can act independently. A towpreg ply is a separate section of towpreg that is substantially more consolidated than the overall towpreg and is separated from neighboring plies for an average axial length of at least about 30 times the thickness of the ply. This geometric separation of non-tacky plies leads to substantially independent flexural deformation of the ply elements. The base flexible multiply towpreg according to the present invention is produced by a three-step process: (1) a tow of reinforcing filaments is spread laterally to expose virtually all of the fibers or filaments to the environment; (2) a matrix material is contacted with the exposed spread filaments in a manner causing interfacial adhesion; and (3) substantial cohesion between neighboring plies within a towpreg is prevented by keeping the plies laterally separated until the matrix material solidifies into a non-tacky state. The base towpreg then can be further processed to form useful products. The flexible multiply towpreg tape according to the present invention is produced by a three-step process: (1) The tow of reinforcing filaments is spread laterally to expose virtually all of the fibers or filaments to the environment; (2) the matrix material is contacted with the exposed spread filaments in a manner causing interfacial adhesion; and (3) the coated tow is forced into a known geometry causing the tow to come together and form a flexible tape of known geometry. The non-woven multiply towpreg fabric according to the present invention is produced by a four-step process: (1) The tow of reinforcing filaments is spread laterally to expose virtually all of the fibers or filaments to the environment; (2) the matrix material is contacted with the exposed spread filaments in a manner causing interfacial adhesion; (3) substantial joining between neighboring plies within a towpreg is prevented by keeping the plies laterally separated until the matrix material solidifies into a non-tacky state, to produce the base towpreg fabric; and (4) forming the base towpreg into the non-woven towpreg fabric of this invention by cohesion methods such as, for example, overlaying, point bonding, or stitching. The flexible recycled plastic matrix towpreg according to the present invention is produced by a three-step process: (1) The substrate of reinforcing fibers or filaments is spread to expose virtually all of the fibers or filaments to the environment; (2) a matrix material comprising recycled plastic is contacted with the exposed spread fibers or filaments in a manner causing interfacial adhesion; and (3) substantial cohesion between neighboring fibers or filaments is prevented by keeping the substrate laterally separated until the recycled plastic matrix material solidifies into a non-tacky state. The base towpreg is produced by supplying a fiber tow consisting of many individual filaments, which are spread or separated from each other, so as to form a lateral spread of individual filaments. The now spread filaments are coated with the matrix forming material. After the filaments are sufficiently coated with matrix forming material, the matrix forming material is liquefied, forming sufficiently wetout fiber tow. As the liquefied matrix forming material wicks down the filaments, the thickness of the matrix forming material becomes thinner until the thin film fractures between filaments. If the tow is sufficiently spread and the spread is maintained, the film will fracture between filaments as the film solidifies. The now coated filaments, either individually or in bundles, are cooled such that the matrix forming material solidifies. During cooling, groups of filaments form individual plies. Sometimes individual filaments link neighboring plies as interply connectors. The plies are pulled so as to keep the fiber tow moving and to place axial tension on the filaments so the individual filaments do not collapse upon themselves, thus forming a mass of filaments and matrix material. The plies can then be gathered together to form various thickness towpregs, which are then wound, or formed into a tape or fabric, or further processed, as deisred. The flexible multiply towpreg tape according to the present invention is characterized by a well-defined overall width and thickness. Typically, flexible multiply towpregs made from fiber bundles are not well-characterized geometrically, leading to difficulties in using such towpregs for processes where an accurate geometry is vital for the production of high quality parts. The tape from flexible multiply towpreg disclosed herein has a well-characterized geometry suitable for processes such as filament winding, advanced tow placement and pultrusion. In a first preferred embodiment, the apparatus for producing the flexible towpreg tape comprises two cooperating rollers, one being generally concave and the other being generally convex, or one having an indented groove and the other having a protruding ridge corresponding to the indented groove, such that the protrusion of one roller fits within the indention of the other roller. A flexible multiply towpreg is passed through a gap of known geometry between the two rollers, forming a towpreg tape of known geometry. In a second preferred embodiment, the apparatus for producing the flexible towpreg tape comprises a single concave roller. A flexible multiply towpreg, under tension, is passed around a portion of the circumference of the roller such that the combination of tension and the concave configuration of the roller forces the flexible multiply towpreg generally toward the lowest point of the concave portion of the roller, thus forming a tape of the proper geometry. The non-woven web of flexible multiply towpregs produced according to the present invention can be used to produce low cost, 2-dimensional fabrics, which can be used for downstream processing into 2-dimensional and 3-dimensional fabrics, preforms, and composite structures. In this regard, the products produced from the flexible fabrics of this invention are less expensive than braided or woven fabrics produced from flexible multiply towpreg. Using this invention, fabrics with matrices that are solid at room temperature can be flexible, whereas conventional technology produces rigid fabrics. The base flexible multiply towpreg of this invention can be used to produce non-woven, flexible, multiply towpreg fabric in which both flexibility and significant fiber wetout is achieved using a solid matrix. Typical fabric structures in which both the matrix and reinforcement are present as fibers (cofiber structures), such as commingled, cobundled, or colayered structures, are flexible, but do not exhibit any wetting of the reinforcing fibers as exhibited in this invention. Therefore, such cofiber fabrics require more intensive processing conditions to consolidate when compared to this invention. To produce the fabric of this invention, the interconnected towpreg plies and filaments forming the base flexible multiply towpreg are overlapped with each other and joined together to form a fabric. Preferably, two or more layers of towpreg are overlapped to form a fabric with a basis weight of between about 50 g/m 2 and about 500 g/m 2 , and preferably between about 150 g/m 2 and about 350 g/m 2 . Various joining techniques are suitable for joining the towpreg plies together, with point bonding by hot melt bonding and line bonding by stitching being preferred. Typically, hot melt bonding of the overlayed towpregs at selected points is used to bond the towpregs together while still maintaining flexibility. Needle punching, entanglement processes and focused pressing also are suitable joining techniques. The matrix material used for the recycled plastic towpreg comprises substantially recycled waste plastic, but may contain virgin plastic. Although all types of plastic may be used as the matrix material, thermoplastics are preferred. Plastic to be recycled first is chopped and then ground to provide a powder. This powder can be partially purified by density separation, if the source of the recycled waste plastic is a mixed plastic waste. The powder is applied and fused to a substrate of reinforcing fibers to produce a prepreg. Composite structures are fabricated from this prepreg in the same manner as conventional prepreg. The substrates preferably are reinforcing fibers in various forms, such as a woven web, a textile fabric or a fiber tow. The reinforcing fibers can be coated as a textile fabric, as well as a spread tow. If a tow is used, towpreg plies typically are produced that are suitable for weaving, braiding, filament winding, formation into tapes and non-woven fabrics, and the like. The primary object of this invention is to provide a flexible multiply towpreg suitable for weaving, braiding, filament winding, pultrusion, tape formation, non-woven fabric formation, and conversion into sheet of bulk molding compound feedstock. A further object of this invention is the production of commercially feasible towpreg from a variety of fibers and matrices. Yet another object of this invention is to provide flexible towpreg containing a sufficient number of filaments to be suitable for the economic production of composite structures. An additional object of this invention is to provide towpreg with the reinforcing fibers sufficiently wetout so that excessive pressure is not required to complete fiber wetout during the consolidation of the composite. Another object of this invention is to produce towpreg rapidly in order to minimize substantial curing or resin advancement of the matrix during towpreg manufacture. Another object of this invention is to permit the production of towpreg starting with the matrix material in the form of inexpensive coarse powders, which are more than twice the diameter of the fibers, or short fibers. A further object of this invention is. the production of commercially feasible towpreg tape from a variety of fibers and matrices. Another object of this invention is to provide a non-woven flexible towpreg fabric well-suited for pultrusion, filament winding, or conversion into sheet of bulk molding compound feedstock, and for fabricating a variety of preforms and composite structures. Yet another object of this invention is to provide non-woven flexible towpreg fabric containing a sufficient number of filaments to be suitable for the economic production of 2-dimensional and 3-dimensional preforms and composite structures. Still another object of this invention is to produce a non-woven towpreg fabric that can be processed in a manner similar to tacky thermoset prepreg tape to layup advanced composite structures. A further object of this invention is to produce a non-woven towpreg fabric that can be used to make bonded preforms for resin transfer modeling, such as tubular preforms, which can be made by tube rolling. Another object of this invention is to provide a towpreg comprising substrate fibers or filaments coated with a matrix material that uses as a primary matrix material recycled plastics. Yet another object of this invention is to permit production of towpregs starting with the matrix material in the form of inexpensive waste plastics. An additional object of this invention is to provide a method for producing towpregs that uses a matrix material that minimizes harm to the processing equipment or the end product. A final object of this invention is to provide towpregs that can be produced from a somewhat mixed or contaminated matrix material source that does not need to be purified but which still results in a composite with satisfactory properties. These objects and others that will become apparent to one skilled in the art are achieved by the present invention as more fully described by the drawings and the detailed description of the invention below. DETAILED DESCRIPTION OF THE DRAWINGS Fig. 1 is an overall flow diagram of the process for producing the base flexible multiply towpreg of the present inven ion; Fig. 2 is a representation of the base flexible towpreg plies of the present invention; Fig. 3 is a comparison of representations of conventional towpreg (Fig. 3a) and the towpreg of the present invention (Fig. 3b); Fig. 4 is a representation of the towpreg plies of the present invention after solidification of the matrix forming material on the reinforcing filaments prior to gathering (Fig. 4a) and after gathering (Fig. 4b); Fig. 5 is a representation of the process of melting the matrix forming material onto the reinforcing filaments of the present invention with lateral constraint (Fig. 5a) and without lateral constraint (Fig. 5b) and a section of the neck of matrix forming material between filaments (Fig. 5c); Fig. 6 is a graph of tow ply thickness versus tow ply modulus of elasticity of varying flexural rigidities for the tow plies of the present invention; Fig. 7 is an overall schematic of the process of the present invention using an electrostatic fluidized bed as the coating system; Fig. 8 is a detailed schematic of the towpreg tape formation means of the present invention; Fig. 9 is a detailed schematic of the towpreg tape formation means of the present invention in an ovenless embodiment; Fig. 10 is a cross-section of the ridged roller and the grooved roller for forming the towpreg tape taken along line 6-6 of Fig. 8; Fig. 11a and Fig. lib are alternate embodiments of the rollers shown in Fig. 10; Fig. 12 is a cross-section of an alternate embodiment of the towpreg tape formation means utilizing a one roller configuration; Fig. 13 is a side view of the one roller towpreg tape formation means shown in Fig. 12; Fig. 14 is a representation of the unidirectional non-woven towpreg fabric of the present invention with Fig. 14a showing the overlaying of towpregs from an axial viewpoint and Fig. 14b showing the point bonding of the overlayed towpregs; Fig. 15 is a representation of the multidirectional towpreg non-woven fabric of the present invention having alternate layers of towpreg oriented in different axial directions, with Fig. 15a showing the overlaying of towpregs and Fig. 15b showing the point bonding of the overlayed towpregs; Fig. 16 is a top view of the unidirectional non-woven fabric shown in Fig. 14b indicating a typical point bonding pattern; Fig. 17 is a top view of the unidirectional non-woven fabric shown in Fig. 14a indicating a typical stitching pattern; Fig. 18 is a micrograph (39. x) of the base tow plies of the present invention; Fig. 19 is a micrograph (lx) of the base towpreg of the present invention subsequent to the solidification of the matrix forming material on the reinforcing filaments but prior to the gathering of the tow plies; Fig. 20 is a 50x photomicrograph of a cross-section of the towpreg tape of the present invention using glass fibers impregnated with polypropylene under 0 psi; Fig. 21 is a 50x photomicrograph of a cross-section of the towpreg tape of the present invention using glass fibers impregnated with polypropylene under 20 psi; Fig. 22 is a 200x photomicrograph of a cross-section of the towpreg tape of the present invention using glass fibers impregnated with polypropylene under 20 psi; Fig. 23 are photographs of the tape of the towpreg tape according to the invention using polypropylene matrix material and glass fiber reinforcing filaments; and Fig. 24 is a photograph of a non-woven towpreg fabric according to this invention made by interleaving a binder filament. DETAILED DESCRIPTION OF THE INVENTION 1- General An important feature of this invention is the promotion of fiber or filament wetting or wet-out, while minimizing the coalescence between wetted neighboring filaments. To prevent coalescence between coated filaments, it is necessary to keep the filaments separated until the matrix solidifies. One approach to keep the filaments separated is by restraining the lateral contraction of the filaments by maintaining an axial tension on the filaments. Fig. 5 illustrates the melting of a matrix material particle supported by two filaments. In Fig. 5a, a high axial tension constrains the filaments from approaching each other. In Fig. 5b, the axial tension on the filaments is low; hence, the filaments can approach each other laterally as the matrix material particle melts and wicks along the filaments. In Fig. 5b-(c), the thickness of the melt between the two filaments is large even after the filaments are substantially wetted. By comparison, in Fig. 5a-(c) the thickness of the melt between the two filaments is substantially thinner than in Fig. 5b-(c) due to constraining the lateral movement of the filaments. Consequently, it is easy to separate the two coated filaments by fracturing the thin film between the two filaments. The result of this separation process is shown in Fig. 5a-(d) . Due to the constraint of the filaments, a tensile stress develops normal to the filament axis in the necked down melt between the filaments. This condition is illustrated in Fig. 5c. This tensile stress develops because material is drawn away from this interfilamentary area in order to spread along the filaments. The neck will fracture if this state of stress, σ N , exceeds the failure stress, σf, for the melt. The failure stress of the matrix can be used as a guide to determine suitable operating conditions for a particular matrix. For example, it is well known that low molecular weight molten materials have virtually negligible tensile failure stresses. It is also known that high molecular weight molten polymers lose strength as their operating temperature is increased. Similarly, partially solvated or plasticized polymers have lower tensile strengths than neat polymers. The thinness of the spread towpreg makes it possible to melt the polymer in a very short time period, and the polymer can be raised well above the normal safe temperature for the melt. In this manner, an extremely low elastic strength in the melt can be achieved to facilitate splitting the towpreg into multiple plies. Conventional matrix forming material systems may operate at a temperature at or slightly above the melting temperature of the particular matrix forming material. The coating system of the present invention can operate at a temperature significantly higher than the softening temperature of the particular matrix forming material, and generally can operate at a temperature as high as the particular matrix forming material will withstand without incurring degrading reaction or resin advancement during the residence time within the system. The residence times used in this invention can be short enough such that no matrix forming material degradation or resin advancement is apparent. The temperature at which the oven or heater operates is related to the residence time of the substrate/matrix material in the oven or heater — high temperatures can be used if residence time is reduced, and vice versa. In this manner, temperatures higher that the temperature at which the matrix material incurs degrading reaction or resin advancement occurs can be used, so long as the residence time is sufficiently short such that the matrix material does not remain at such a temperature for a length of time sufficient to allow the matrix material to incur degrading reactions or resin advancement. The same conditions that lead to lower tensile strength in a viscoelastic liquid lead to lower surface tension and lower viscosity for the liquid. Thus, the same conditions that promote filament separation also promote spreading of the liquid along the filaments. Thus, the conversion in liquid shape depicted in Fig. 5a can be physically realized by manipulating material and operating conditions such that the elasticity of the liquid is minimized. By constraining or preventing the lateral contraction of the filaments towards each other, the length of the neck before fracture, L n , can be minimized. Then thinning of the cross-sectional area, A n , is promoted and the force, F n , required for fracture is reduced. Thus, maintaining a high degree of tow spreading throughout wetting and solidification promotes separate filament coating. Fracture of the liquid film between filaments can be facilitated by additional forces. Hot gases blown normal to the plane of the spread tow will promote interfilament film fracture. Running the spread tow over grooved rolls, such that the filaments are forced toward the roll axis, will facilitate splitting interfilamentery films. A variety of mechanical devices can be introduced to assist filament separation like the grooved rolls. In order to produce the base towpreg of this invention, substantial wetout of the fibers by the matrix material must be accomplished such that the matrix forming material has been liquefied sufficiently to achieve adhesion to the filaments without the use of a conventional adhesive or binder. Wetout typically is accomplished via a matrix material liquefier, such as a melter or oven, which, through heat, puts the matrix material into a liquid state. To achieve substantial wetout, sufficient residence time in the apparatus selected to put the matrix in a liquid state and to allow the matrix material to sufficiently wetout the fiber is required. There are various liquefiers available, including any of the radiation or conduction ovens. Radiation ovens are preferred for dry powder. Additionally, a hot die can be used in place of an oven. Because the matrix material is liquefied as part of this invention, it is possible to use any size particles of matrix material powder to coat the filaments, including coarse particles and short fibers. The liquefaction of the matrix material and the wicking of the matrix material along the filaments reduces the problem of coarse blending between matrix material and filament associated with applying large diameter particles to small diameter filaments. Therefore, the particle size of the matrix forming material in this invention is not critical and can range from the diameter or thickness of the filaments or smaller, which is the generally accepted size in the art for coating, to a diameter or thickness many times larger than that of the filaments, including short fibers, as in the present invention. The use of large diameter or thickness particles of matrix forming material which, until the process of the present invention, had not been used with any success, also results in significant cost savings. 2. Preferred Materials The various fibers that are useful as the tow fibers or filaments include glass fibers; carbon and graphite fibers; organic fibers, particularly liquid crystal fibers such as aramids and aromatic polyesters which are not low melting; ceramic fibers, such as silicon carbide; hybrid fibers, such as aramid/carbon, aramid/glass, aramid/carbon/glass, and carbon/glass fibers. In general, fibers with a diameter or thickness greater that 25 microns are not useful. For example, there is no point in using a boron fiber with a diameter of 140 microns, as fibers of that thickness cannot be made very flexible. Further, the fiber chosen should be a reinforcing type fiber and available in continuous form. Suitable fibers should be thermally stable at the temperatures involved in the matrix consolidation step. Additionally, suitable fibers must have glass transition and melting temperatures greater than room temperature and melting temperatures greater than the consolidation temperature of the composite. Both thermoplastic and thermoset polymers are suitable for use as matrix materials. Preferred polymers generally should not be tacky and should have a glass transition or melting temperature greater than room temperature while in service and after curing. Preferably, the glass transition temperature should be greater than room temperature. Therefore, elastomers, rubbers, and leathers, which are not rigid at room temperature, are unsuitable for use as the matrix material. Thermosets, which can be tacky at process temperatures, can be processed cold to reduce tackiness and increase suitability as matrix materials. Non-polymer materials, such as copper, low melting point metals, and ceramic precursors also may be used as the matrix materials. The matrix material can be of any configuration, such as particles, powders, and short length fibers. Example classes of polymers are the ABS group, acetals, acrylics, alkyd polyesters, allyls, aminos, epoxies, fluoroplastics, furans, melamines, nylons, phenolics, phenylene oxides and ethers, polyamides, polyamide-imides, polybutylenes, polycarbonates, polyesters, polyetheretherketones (PEEK), polyetherketones (PEK), polyetherketoneketones (PEKK) , polyetheri ides, polyethylenes, polyimides, polymethylpentenes, polyphenylene sulfides, polypropylenes, polystyrenes, polyurethanes, sulfones, ureas, and vinyls. Copolymers, alloys, and blends can be suitable polymer matrices. Within these classes of polymers, specific grades that are not tacky immediately following solidification after the creation of a multiply towpreg are preferred. In addition, thermosetting polymers should not be fully cured when the towpreg is initially solidified in order to permit bonding between the plies and tows when the composite part is finally cured. The preferred polymers for use as the matrix material include engineering polymers, such as polyetheretherketones, polyamides, epoxies, and polyesters. The preferred matrix material for use in producing the recycled plastic towpreg comprises substantially recycled waste plastic. Blends of recycled plastics and blends of recycled and virgin plastics also are suitable. Although any type of plastic may be used as the matrix material, thermoplastics are preferred. Plastic to be used as matrix material preferably is first chopped and then ground to provide a powder. This powder can be partially purified by density separation if the source of the recycled waste plastic is a mixed plastic waste, or contains virgin plastic, or both. The powder is applied and fused to a substrate of reinforcing fibers to produce a prepreg. Towpreg and composite structures are fabricated from this prepreg in the same manner as conventional prepreg. Recycled plastic containing towpreg does not have to be flexible to be useful, and the present invention is capable of producing towpregs with a wide variety of flexibility ranges. The combination of the use of any quantity of recycled plastic in the matrix material and reinforcing fibers is inherently useful with any degree of flexibility. By using recycled plastic, the cost of the matrix is considerably less when compared to other materials. Recycled plastics sometimes contain infusible materials which can be embedded in the towpreg product with little harm to the processing equipment or product. The plastic is not melted in an extruder with close tolerances but in a noncontact oven; therefore, infusible material will not harm the processing equipment. As the properties of the towpreg and composite products are dominated by the reinforcing fibers, a somewhat mixed or contaminated matrix can be tolerated. Thus, by means of this invention, the recycled plastic does not have to be purified to a great extent to achieve suitable towpreg or composite properties. Different plastics typically are incompatible with each other and, therefore, mixed plastics typically have low physical properties. Industrial plastic scrap often is segregated and is a preferred source for recycling. Post-consumer plastic is mixed to varying degrees depending on the collection program. For example, mixed in with PET bottles are non-PET bottle caps, paper labels, and other types of bottles and consumer plastics. Thus, a PET source probably only is about 80% PET. In the past, the other 20% was a problem, which led to expensive purification processes. In this invention, a large percentage of these contaminants can be tolerated. For example, a typical towpreg may comprise 50% fiber, 40% PET as matrix material, and 10% contaminants. As the fibers dominate the properties of the towpreg and any composite made from the towpreg, a comparatively high percentage of contaminants can be buried in the towpreg as harmless filler. The prefered recycled plastics are thermoplastics, as the main focus for recycled plastics are the thermoplastics, although other types of plastic may be used. Mixed thermoplastics or combinations of thermoplastics also are suitable for use as the matrix material. Typically, cured thermoset materials without chemical treatment are used essentially as fillers. Additionally, blends of recycled plastics and virgin plastics may be used, and may be more appropriate for commercial applications. 3. Characteristics of Towpregs ASTM D 1388 is a standard test method used to determine the stiffness of fabrics. This standard can be used to characterize the stiffness of the towpreg. Generally, a standard sample is 1 inch wide; however, measurements can be made on samples less than 1 inch wide, as long as the results are corrected for this difference. ASTM D 1388 is incorporated herein by reference. A standard thermoplastic prepreg, such as APC 2 made by ICI, is 5 mils or 127 microns thick and has a flexural rigidity estimated to be 216,000 mg-cm. A towpreg with this flexural rigidity is very difficult to weave, braid, or form into a tape or flexible fabric and, thus, a thinner towpreg is preferred; that is, a multiply towpreg with an average ply thickness less than about 50 microns. Such towpregs are produced by this invention. Flexibility is important for weaving fabrics and forming tapes and non-woven fabrics. The cantilever test method, ASTM D 1388-64 (1975), incorporated herein by this reference, is used to calculate the flexural rigidity by measuring the bending length of the towpreg. Bending length is a measure of the interaction between the weight of the towpreg and its stiffness as indicated by the way in which a towpreg bends under its own weight. It reflects the stiffness of the towpreg when bent in one plane under the force of gravity, and is one component of drape. The maximum elastic strain in the towpreg is at its surface. Reinforcing fibers typically cannot withstand compressive strains beyond 0.3% without buckling. For an elastic ply, this strain can be related to the ply thickness and minimum bending radius through the following expression: h = 2R min e where: h = the ply thickness R min = P-*- y bending radius e = maximum allowable surface strain. For example, a ply subjected to a minimum bending radius of 10 mm and a maximum allowable strain of 0.3% cannot be more than 60 microns thick. The minimum bending radius depends on the part geometry and the maximum strain depends on the reinforcing fiber. Thus, ply thickness depends on both the material and application. This is shown graphically in Fig. 6. 4. Producing To preαs and Products The method for producing the base towpreg is shown in a simplified flow process chart in Fig. 1. This method should be read in conjunction with the more detailed description disclosed below in the description of the preferred apparatus. The tow 102 is supplied during the let-off step 101, which can be bobbins or spools of tow, tow from an upstream process, or from any other tow supply. The tow 102 consists of many individual filaments 104, which are spread or separated from each other, so as to form a lateral spread of individual filaments 104, in the spreading step 103. A spread of about 2 inches is typical for a 6000 filament tow. The now spread filaments 104 are coated with the matrix forming material during the coating step 105. After the filaments 104 are sufficiently coated 106 with matrix forming material, the matrix forming material is liquefied in wetout step 107, forming sufficiently wetout fiber tow 108. As the liquefied matrix forming material wicks down the filaments 104, the thickness of the matrix forming material becomes thinner until the thin film fractures between filaments 104 (see Fig. 5) either before or during the splitting step 109. If the tow 108 is sufficiently spread and the spread is maintained, a splitting step 109 is not necessary, as the film will fracture between filaments 104 as the film solidifies. In addition, for a well-spread tow, the resin film will not bridge multiple plies; hence, interply fracture of the film may not be requires. The now coated filaments 110, either individually or in bundles, are cooled in the cooling step 112 where the matrix forming material solidifies. During the cooling step 112, groups of filaments 110 form individual plies 113. Sometimes individual filaments 110 link neighboring plies 113 as interply connectors 111 during the cooling step 112. The plies 113 are pulled by a pulling means 114 so as to keep the fiber tow 102 moving and to place axial tension on the filaments 104 so the individual filaments 104 do not collapse upon themselves, thus forming a mass of filaments and matrix material. The plies 113 can then be gathered together 115 to form various thickness towpregs, which are then wound in winding step 116, or formed into a tape or fabric 139, or further processed, as deisred. The production of a towpreg tape is accomplished by guiding the coated tow into a gap of known geometry causing the tow to come together in the gap and form a flexible tape of known geometry. Referring now to Figs. 8 - 13, in a first preferred embodiment the apparatus for producing the flexible towpreg tape comprises two cooperating rollers, shown in Figs. 10 and 11, one being generally concave and the other being generally convex, or one having an indented groove and the other having a protruding ridge corresponding to the indented groove, such that the protrusion of one roller fits within the indention of the other roller. A coated tow is passed through a gap of known geometry between the two rollers, forming a towpreg tape of known geometry. The rollers typically are forced together under a known pressure by conventional mechanisms, such as an air cylinder, springs, or hydraulic cylinders mounted on one of the rollers. The rollers are placed at the output end of a coating line, or as a replacement for the fusion oven of a fusion coating line. In a second preferred embodiment, the apparatus for producing the flexible towpreg tape comprises a single concave roller, shown in Figs. 12 and 13. A coated tow is passed around a portion of the circumference of the roller. The coated tow is kept under tension as it passes around the roller such that the combination of tension and the concave configuration of the roller forces the coated tow generally toward the lowest point of the concave portion of the roller, thus forming a tape of the proper geometry. The tension can be created on the coated tow by the, for example, wind up rollers elsewhere in the apparatus. The single concave roller also is placed at the output end of a coating line, or, if heated or if enough pressure is created, as a replacement for the fusion oven of a fusion coating line. Alternatively, flat circumference rollers can be used to produce the towpreg tape. The production of a non-woven fabric from the towpreg is discussed in connection with reference to Figs. 14 - 17. The plies 113, interply connectors 111, and individual filaments 110 together makeup an individual towpreg 133 comprising reinforcing filaments 132 coated with matrix forming material 131. After the towpregs 133 are cooled in the cooling step 112, the towpregs 133 are arranged in a desired fabric pattern, such as the unidirectional overlap pattern shown in Fig. 14a or the multidirectional overlap pattern shown in Fig. 15a. Preferably, the arrangement of towpregs 133 comprise the overlapping of the towpregs 133 so as to increase the strength of the resulting fabric 139. Once the towpregs 133 are properly arranged, the towpregs 133 are joined together. Hot melt bonding of the overlayed towpregs 133 at selected points results in the point bonded fabric 139 shown in Fig. 14b and Fig. 15b. One or more point bonds 137 are used to bind the towpregs 133 together. Using point bonding rather than continuous bonding of towpregs 133 to each other results in a fabric 139 which maintains flexibility. Alternatively, stitching 138, needle punching, pressure point bonding, or water-jet impingement can be used to join the towpregs 133. A representation of such a stitch pattern is shown in Fig. 17. The stitching can be done at an angle to the direction of travel of the towpregs 133 to facilitate continuous processing. The non-woven fabrics of this invention do not have interleaved reinforcing fibers; however, binder filaments or yarns may interleave the reinforcing fibers as shown in Fig. 24. In this case, the hydrid fabric is woven, but the assembly of reinforcing fibers is non-woven. The resulting fabric 139 then can be wound in a winding step for further use. Alternatively, the towpregs 133 or the resulting fabric 139 can be acted upon so as to create 2- and 3-dimensional non-woven fabrics and even preforms having complex contours. For example, tubular preforms can be made by multiaxial layup or tube rolling, a common practice for fabricating golf club shafts, tennis rackets, and sailing masts, among other structures. To achieve substantial wetout, sufficient residence time is required in the apparatus selected to put the matrix in a liquid state and to allow the matrix material to sufficiently wetout the fiber. It is important that during the wetout stage the fibers or filaments are not allowed to collapse laterally. This is prevented by maintaining sufficient tension on the tow. After the fibers or filaments have been substantially wetout, the liquefied matrix material generally coats an entire bundle of fibers or filaments. In order to produce the towpreg of this invention, groups of fibers must be separated from each other as shown in Fig. 2 so as to produce individually coated multiple plies within a tow. With reference to Fig. 2, the individually coated multiple plies, represented generally as 134, are composed of reinforcing filaments 132 and matrix forming material 131. Although entirely individual plies 134, such as represented generally by 136, are ideal, the plies 134 can be connected to each other by interply connectors 135, which are generally single filaments 132 coated with matrix forming material 131. These coated plies have a lower flexural rigidity than fully consolidated towpreg. With reference now to Figs. 3 and 4, in conventional towpreg production, tows containing bundles of generally about 800 to 13,000 filaments 132, each filament 132 having a diameter or thickness of generally about 4 to 16 microns, are converted to towpregs 130 by coating with matrix forming material 131. The conventional process yields a towpreg "ply" 134 of about 1/8 to 1/2 inch wide. The term "ply", as used in the conventional process, indicates an individual, conventional single-ply towpreg 130 that can be used alone or with other conventional single-ply towpregs 130 to form composite structures. The "plies" 134 of the present invention are individual, substantially wetout bundles of filaments 132, each bundle or "ply" having an average thickness of 100 microns or less and preferably less than 50 microns, which are gathered to form a "multiply" towpreg 133 of any desired thickness. Splitting occurs, or is maintained, if the filaments 132 are well spread by the tow spreader and are held in sufficient tension throughout the process such that the fibers or filaments 132 cannot collapse laterally onto each other. Splitting can occur before or concurrently with wetout in the oven 16 as it generally occurs as the liquefied matrix material 131 wicks longitudinally along the axis of the filament 132. Various alternative methods of splitting can be employed, such as the addition of mechanical separators, including grooved rolls, knives, laser cutters, and convection currents perpendicular to the spread tow. A single towpreg 130 contains several plies 134, which vary in thickness and width. The average thickness of the ply 134 is less than 100 microns and is preferably less than 50 microns. The maximum thickness of the ply 134 is about 100 microns and the minimum height of the ply 134 is the diameter or thickness of an unimpregnated fiber 5 132 used as the reinforcing filament in the ply 134. Typically, the length of a ply 134 is greater than the width of a ply 134 and both the length and width of a ply 134 are greater than the thickness of a ply 134. Generally the thickness of a ply 134 is much less than the width of a ply 134, which is generally less than 2000 microns. Additionally, the average length of a ply 134 is preferably greater than 30 times the thickness of a ply 134. 5. Preferred Apparatus It should be noted that the above steps define the method of this invention and are not to be limited to the specific examples given throughout this specification. However, to better understand the above steps, the example below is provided with reference to the specific apparatus 8 shown in Fig. 7. Referring now to Fig. 7, the tow 11 supplied on let-off wheel 10 is drawn through the apparatus 8 and secured to take-up wheel 12. The take-up wheel 12 is rotated at a variable speed and the let-off wheel 10 is not necessarily driven. Typical linespeeds are 3 to 30 meters per minute. Slower speeds are feasible but are not economically attractive for a number of reasons including, for example, less towpreg produced per time unit and the chance that the matrix forming material will be destroyed through degradation or resin advancement due to increased oven residence time. Higher speeds can be achieved provided tow supports are installed to minimize tow vibration, the matrix applicator is long enough to ensure sufficient matrix is applied, and the oven is long and hot enough to liquify the matrix. Line speeds above 30 meters per minute are feasible in some cases under proper conditions. Intermediate pinch rollers 14 are used to pull the fibers 11 as they come out of the oven 16, A constant tension winding on take-up wheel 12 is maintained by adjusting the winder motor (not shown) speed with a tension controller (not shown) . The tow speed through the apparatus 8 can be controlled by adjusting the speed of the pinch rollers 14. The tow let-off in this example is taken directly from bobbins of wound fibers. The fiber tow also can come directly from upstream processes. During let-off, it is important to avoid twisting the filaments 13 making up the tow 11 as twisted filaments 13 are more difficult to separate. Additionally, it is helpful to control the tension on each individual bobbin of tow to keep the line tension constant throughout the impregnation process. A tow guide plate (not shown) may be placed between the let-off mechanism and the tow spreader 18 to aid in guiding the tow through the tow spreader 18. The tow spreader 18 in this example uses a series of rollers 17 and an air comb 19 to spread the tow 11 to individual filaments 13. The rollers 17 typically are arranged in two groups of rollers; one group located just before the air comb 19 and one group located just after the air comb 19. The two main purposes of the rollers 17 are: (1) to provide tension to the tow thus reducing the amount of lateral collapse of the tow onto itself during the process; and (2) to reduce the vibration of the tow. The rollers 17 can be made of any suitable material and have any surface characteristics; however, smooth Teflon rollers are preferred as they provide for good spreading of the tow. At least one of the rollers 17, preferably the one immediately before the coating system 20, must be made of a conducting material, stainless steel being preferred, so as to ground the tow 11 before it enters the coating system 20. The air comb 19 already is known in the art. The tow 11, after leaving the let-off wheel 10, enters the first group of rollers 17 where the filaments 13 are spread. The configuration of this first group of rollers 17 allows the tow 11 to weave through the first group of rollers 17, passing over and under the consecutive rollers, helping to impart a constant tension on and to reduce the vibration of the tow filaments 13. The tow 11 then enters the air comb 19 where forced air further spreads the filaments 13. After leaving the air comb 19, the tow 11 enters the second group of rollers 17 where the filaments 13 are further spread. For example, a 3000 filament tow typically is spread more than 1 inch wide in order to maintain a flexible towpreg. The configuration of this second group of rollers 17 is similar to the configuration of the first group of rollers 17 for the same reasons. It is preferred that the final roller in this second group of rollers also be made of a conducting material so as to ground the fibers prior to entering the coating system 20. Various other tow spreader 18 means are available, including smooth, grooved or crowned rollers or drums; air combs; a combination of air combs and rollers or drums; air banding jets; ultrasonic spreaders; and liquid baths. Of prime concern in choosing tow spreading means is that the means chosen will spread the tow into a columnated tape preferably only one filament thick, and that the means will not damage the fibers or filaments. Additional subprocesses may be included between the tow spreader 18 and the coating bed system 20 as required in the various applications. For example, equipment for desizing, surface activation and application of adhesion promoters may be desired to produce a towpreg desired for a specific application. The tow filaments 13 next enter a coating system 20 where the matrix material is applied to the . tow filaments 13. As the tow filaments 13 enter and pass through the coating system 20, the spread of the tow filaments 13 is maintained. Many different coating systems 20 are useful and are discussed as examples below. Powder spray coating systems and electrostatic fluidized bed systems are preferred, powder spray coating systems typically being less costly to operate. Various other coating systems 20, such as wet powder, hot melt, and solution coating also can be used. a. Fluidized Bed. The fluidized bed coating system 20, in its simplest embodiment, comprises an enclosure 21 within which the matrix material powder 22 is confined. By a combination of air flow 24 and mechanical vibration, the powder 22 is fluidized and simultaneously electrically charged by means of high voltage electrodes 26 situated at or near the base of the container 28. The electrode 26 may consist of sharp points or, more usually, small diameter wires. At the top of the coater enclosure 21, there is an open port 32 to allow the escape of the fluidizing air 24. Passing the towpreg fiber substrate over and under rollers connected to a metal frame is one procedure to simultaneously ground and spread the fibers. With greater spreading, more powder can be picked up and greater flexibility of product results because the substrate is thinner. When the fibers are not spread prior to coating, the towpreg emerges in a brittle state and the fibers within the towpreg are not totally coated. The powder particles 22 are uniformly dispersed in the container 28. For electrostatic coating, a preferred particle size range is about 20 to about 80 microns, with an average particle size of about 50 microns. Flexible towpreg has been produced from both finer and coarser powders. Particles less than about 20 microns have been applied successfully, although it is likely that these fine powders, especially those less than about 10 microns, agglomerate into larger particles in the fluidized bed. Coarse particles up to about 250 microns have been applied, but the flexibility of the towpreg is reduced as the size of the applied powder is increased. Short fibers also can be used as the powder 22. As recycled plastic powders are most conveniently obtained by grinding and the cost of grinding increases as the average particle size is reduced, it is preferable to select coarse powder. The coarseness of the powder must be counterbalanced by the flexibility and extent of mixing desired in the towpreg for downstream processing. The porous plate 34 provides for a very high resistance to travel of air 24 through the plate 34 while permitting passage of sufficient air 24 at low velocity to fluidize the powder 22. Mechanical vibration of the porous plate 34 is used to enhance fluidization and to reduce the possibility of air channeling and powder clumps. The depth of powder material 22 in the bed 33 is usually two to four inches (50 to 100 mm). In the fluidized bed system 20, individual particles of the powder 22 electrostatically adhere to the fibers. The charged particles of powder 22 repel each other to such a degree that they rise above the chamber container 21 forming a cloud 40 of charged particles, through which the fibers are passed. In this example, a model C30 electrostatic fluidized bed coater from Electrostatic Technology Incorporated is used. The bed dimensions are 15 x 15 centimeters. The electrical output is 0-90 kV and the air input is 0-0.4 standard cubic meters per minute. The fluidized bed system 20 also incorporates an ionized air system 36 created by charging electrodes 26 below the fluidized bed 33 to prevent the unintentional ignition of the fluidized powder 22 by electrical sparking. The fluidizing air 24 must be dry and clean because contaminants within the air supply would result in blocking the porous plate 34 and uneven fluidization. Moisture in the air causes the powder 22 to pack on the fluidized bed 33, causing reduced fluidization efficiency. Normally dry air 24 at a pressure of 200 to 700 kPa supplied at a rate of approximately 1.5 m 3 /min per m 2 of diffuser plate 34 is appropriate. The fluidized powder 22 is maintained in the fluidized state by controlling the air flow 24. A typical method for drying the fluidizing air 24 is to use a cylindrical chamber (not shown) filled with silica gel, such as Drierite. Alternatively, the air can be dried by refrigeration. Wet air enters the dryer and moves through a mesh screen into the silica gel. Moisture is separated out in the chamber. Dry air 24 then flows through the outlet to the fluidized bed 33. The voltages employed in the fluidized bed system 20 are usually between about -30 to about -100 kV. In most cases, negative polarity is used. The output voltage should be approximately -100 kV maximum and the maximum output energy when the system 20 is shorted to ground must not be greater than the ignition energy of the particular materials 22 being applied. The high voltage required depends on the powder being used and generally ranges from about -35 to about -90 kV. For example, polyester powders achieve a better coating when charged at -40 kV or less; epoxy powders perform well in the range from -40 to -70 kV; vinyl powders generally require a higher charge, on the order of -60 to -75 kV; and for PEEK, good powder pickup occurred at -70 to -90 kV. A vacuum exhaust system (not shown) is positioned to collect and return the excess coating powder to the powder supply reservoir (not shown) . A typical exhaust system consists of one or more cyclones or bag filters (not shown), or a combination of both. Top exhaust, entrance and exit port exhaust or perimeter exhaust are all techniques that can be applied. The velocity of exhaust air should be about the same as the velocity of the inlet air flow 24. In this example, the exhaust system employs a cartridge type exhaust to recover powder by collecting the powder in a vacuum bag filter. Powder is drawn to the cartridge by air suction, and then recovered by shaking the pocket or the bag filter inside the cartridge. Typical residence times in the powder coating chamber are from about 1 to about 5 seconds. This time depends on the type of fiber, the extent of fiber spreading, the type of plastic, the particle size, the coater operating conditions (e.g., air flow and electrostatic charge) , and the amount of matrix sought in the towpreg. The coated fiber next enters the oven 16 as shown in Figs. 1 and 8, or is introduced directly to a ceramic or other heater 70 as shown in Fig. 9. This should be accomplished as soon as it leaves the fluidized bed system 20 in order to melt the powder 22 onto the fibers before the decay of charge or charge relaxation occurs and the powder falls off the fibers. The oven 16 or heater 70 temperature depends on the fiber and the powder 22. However, oven 16 or heater 70 temperature and residence time within the oven 16 or heater 70 should be set to insure that the decomposition temperature of the powder 22 resin is not achieved for the residence time the coated fibers are in the oven 16 or heater 70. The oven temperature should be sufficiently high to melt the highest temperature plastic present. The coated fibers can be heated by either convection or radiant heating. In this example, the oven 16 is a Lindberg single zone tube furnace, which has a maximum operating temperature of 1200°C, is 75 cm in length, and has an inside diameter of 5 cm. Typical residence times in the oven for the towpreg are about 2 to about 20 seconds. In most cases, a residence time of less than about 10 seconds is adequate for liquefying and fusing the plastic to the fibers. For viscous melts, such as high molecular weight polyethylene, longer times may be required to promote wicking along the fibers. Radiant or convection heating is suitable. Typically in post-consumer plastic recycling polyethylene terephthalate (PET) is the highest melting plastic. As PET melts near 250°C, an oven setting of at least the melting temperature of PET, about 250°C, and preferably 300°C or more, is desired. In order to reduce the oven residence time and enhance wetout, much higher oven temperatures can be used because the material temperature does not reach the oven temperature. When the oven temperature is above about 400°C, which will cause most recycled plastics to degrade given sufficient residence time, provision must be made to remove powder that drops off of the tow into the oven. Without this provision, the potential for creating a fire is increased. b. Powder Spray Coating Powder spray coating of the fibers by the matrix material particles can be accomplished using an electrostatic or tribostatic (tribocharging) spray gun. In its simplest design, an electrostatic spray gun is a tube with a charging electrode attached to a high-voltage generator. Powder particles are directed through the gun tube, typically by a forced air flow, and charged by the electrode. The charged powder particles are directed at the substrate, in this case the fibers, where they adhere to and coat the substrate. The substrate is grounded such that an opposite charge relationship is created between the charged powder particles and the substrate. In the present example, the electrostatic spray gun is contained within a powder chamber, which replaces the fluidized bed. The fibers leave the spreader and enter the powder chamber. Matrix material as powder is fed to the spray gun where it is charged and directed at the fibers, which are grounded. Some charged powder particles adhere to and coat the fibers, while the remainder is recycled to the spray gun. The coated fibers exit the powder chamber and proceed to the oven. The air flow through the spray gun, the powder flow input, and the electrostatic control are all variable and values are selected based primarily on the fiber and matrix material being used. For example, using a Ransburg-Gema AG unit type 701-6 electrostatic spray gun to coat 12K carbon fibers spread to 5 cm with less than 150 micron nylon 11 powder with some carbon black pigment, various settings can be used to accomplish coating. The Ransburg-Gema unit allows an air flow "level" of 0-7, a powder flow "level" of 0-10, and an electrostatic setting of 0 - -80kV. The following Table I presents example coating parameters and values. TABLE I Coating Values Line Speed Air Flow Powder Electrostatic % Matrix (m/min) Level Flow Level Setting (-kV) Bv Weight 3.54 1.5 4.5 25 34.8 6.21 2.0 6.0 15 41.0 8.25 2.0 10.0 7 43.5 13.65 2.0 10.0 7 30.0 c. Wet Powder Coating In wet powder coating, the matrix material is a wetted powder, such as a slurry or emulsion coating. In wet powder coating, there is no need to ground the fiber tow prior to entering the coating system 20; therefore, the stainless steel roller 17 mentioned above is not necessary. After leaving the spreader 18, the fibers are drawn through an optional primer for applying an adhesion promoter. After leaving the primer, the fibers travel into the wet powder coating system proper, which comprises a roll coater, a wet powder or emulsion reservoir, and a slurry pump. The matrix material is suspended in a liquid medium that can be either water or solvent based. The water based medium includes water and, possibly, a water soluble binder, and the solvent based medium contains a solvent and, optionally, a dissolved binder. The fibers travel over the top surface of the roll coater that rotates generally in a direction complimentary to the direction of fiber travel. The lower surface of the roll coater contacts the slurry or emulsion in the reservoir and becomes coated with the slurry or emulsion. As the roll coater rotates, it brings the slurry emulsion to its top surface where it contacts and coats the traveling fibers. The slurry pump maintains the slurry or emulsion in a uniform concentration. The coated fibers leave the roll coater area and enter a drier where the water or solvent is evaporated from the slurry coating the fibers. The water soluble binder may be removed provided the resin is fused to the fibers. The now dry fibers leave the drier and enter a melter where the matrix material is liquefied and wets the fibers. An alternative to using a roll coater in the wet powder coating system is to draw the fibers directly through the slurry or emulsion itself. After being drawn through the slurry or emulsion, the fibers then travel directly to the drier. d- Hot Melt Coating. A hot melt system typically comprises a roll coater or an extruder and die. The hot melt system utilizes the roll coater, and operates in the same manner as the wet powder coating system described above, with the exception that the slurry or emulsion reservoir is replaced with a melt reservoir containing the hot melt of the matrix material. As in the wet powder coating system, the roll coater is optional as the fibers can be drawn directly through the hot melt reservoir. The hot melt coating system utilizing the extruder and die operates by pulling the spread fibers through a slit die supplied with hot melt by an extruder. The matrix material coats the fibers in the die. The die land is grooved to facilitate splitting the towpreg into multiple plies. Fiber wetout starts as soon as the hot melt of the matrix forming material contacts the fibers. Therefore, an oven to accomplish further wetting may not be necessary. Special provisions, such as a grooved die or roll coater, may be necessary to facilitate splitting the towpreg into multiple plies. e. Solution Coating. Solution coating systems utilize various solvents. In this system, the matrix material is dissolved in an applicable solvent and the fiber tow is drawn through this matrix material/solvent solution or over a solution coated roller so as to coat the fibers. The coated fibers are then passed through a drier to evaporate the solvent. 6. Sample Towpregs a. Carbon fiber tow filament /PEEK matrix material. Unsized 6K Hercules AS4 carbon fiber tow, each carbon fiber filament having a diameter of 8 microns, passes through an air banding jet that spreads the tow to about 60 mm wide. Rollers before and after the spreader create tension in the tow. The tow passes over an electrostatically charged bed containing PEEK 150 PF powder from ICI with an average particle size of 90 microns. The tow is grounded and the powder is charged at about -65 kV. The tow passes in spread condition under lateral tension, to prevent collapse, through a tubular oven set at 450°C to melt the PEEK. The tow is cooled in air and passed through drive rollers to a tension controlled winder. The residence times in the powder coater and the oven are 1.4 and 6.7 seconds, respectively. The line speed is 6.8 meters per minute, the fiber content of the towpreg is 60% by volume. The towpreg flexural rigidity is 890 mg-cm compared to 670 mg-cm for the uncoated tow. By comparison, consolidated towpreg has an estimated stiffness of 216,000 mg-cm. b. Glass tow filaments/PEEK matrix material. A towpreg comprised of Owens Corning Fiberglas high temperature sized S2 glass with 4,080 filaments, each glass filament having a diameter of 9 microns, impregnated with PEEK matrix material is produced as in a. above. After the glass filament tow passes through the air banding jet, the tow is wiped, preferably just before the last, grounded, roller by a wet sponge to " improve surface conductivity. Then the tow passes over the electrostatically charged bed containing the PEEK 150 PF powder from ICI with an average particle size of 90 microns. The tow is grounded and the powder charged at about -70 kV. The tow passes, in a spread condition under lateral tension to prevent collapse, through the tubular oven set at 450°C to melt the PEEK. The tow is cooled in air and passed through drive rollers to a tension controlled winder. The residence times in the powder coater and oven are 5.2 and 26.3 seconds, respectively. The line speed is 1.7 meters per minute. The fiber content of the towpreg is 60% by volume. c. Carbon fiber tow/LaRC-TPI matrix material. A towpreg comprised of unsized 6K Hercules AS4 carbon fiber tow, each carbon fiber filament having a diameter of 8 microns, impregnated with LaRC TPI, a thermoplastic polyimide, is produced as in a. above. After the carbon fiber filament tow passes through the air banding jet and the rollers before and after the air banding jet, the tow passes over the electrostatically charged bed containing the LaRC-TPI powder from Rogers Corp. with an average particle size of 35 microns. The tow is grounded and the powder charged at about -67 kV. The tow passes in spread condition under lateral tension, to prevent collapse, through the tubular oven set at 400°C to melt the TPI. The tow is cooled in air and then passes through drive rollers to a tension controlled winder. The residence times in the powder coater and oven are 3.2 and 16 seconds, respectively. The line speed is 2.9 meters per minute. The fiber content of the towpreg is 37% by volume. The towpreg flexural rigidity is 7,000 mg-cm compared to 670 mg-cm for the uncoated tow. 7. Post-Coating Treatment of Towpregs a. General After the fibers 13 have been wetout by the matrix forming material in the coating system 20, the towpreg 50 can be passed through an optional set of polishing rollers 46. These rollers 46 can be located within the oven 16 or heater 70 or just after the exit of the oven 16 or heater 70, but, in any event, the rollers 46 must be located in a position on the apparatus 8 where the matrix forming material is still in the liquid state. The purposes of the polishing rollers 46 are to force the still liquid matrix forming material into the tow plies to help achieve better wetout and to reduce the surface friction of the plies due to droplets of matrix forming material being left on and solidifying on the surfaces of the towplies. After leaving the oven 16 or heater 70, the towpreg 50 cools rapidly because the plies comprising the tow are relatively thin. Typically, air cooling is sufficient, although the use of blowers, cold rollers, and the like may be advantageous in certain situations. During cooling, it is important that the spread tow remain in sufficient tension such that the individual plies do not collapse onto each other and result in a mass of fibers and matrix material, which will result in a towpreg of high flexural rigidity. Also, it is important not to let the fibers within the towpreg solidify in contact with each other, thus leading to a strong interply bond. An optional convective cooling method (not shown) located after the oven 16 or heater 70 would help keep the plies separated. Conductive cooling methods may be used as they require surface contact, which constrains the lateral motion of the tow. Splitting after cooling is possible with mechanical devices such as described above; however, it is inadvisable to rely on doing all of the splitting after cooling, as this would cause an unacceptable amount of fiber damage. Towpregs typically must contain over about 25% matrix material by volume so as to form sufficiently void-free composite structures suitable for processing into final composite structures. The main purpose of the pinch rollers 14 is to drive the tow 11 through the process and to keep sufficient tension on the tow 11 to prevent the tow 11 from laterally collapsing onto itself. The various devices useful for pulling include driven pinch rollers, preferably rubber coated, and friction rollers, also preferably rubber coated. The take-up or wind-up device 12 can be any of the known typical tow winders with a tension control. Alternatively, the towpreg 50 may be fed directly to downstream processes, such as a chopper, to produce sheet or bulk molding compound feedstock. b. Tape To produce towpreg tape, after the filaments 13 have been wet-out by the matrix forming material in the coating system 20, the towpreg 49 is introduced to the tape formation region 109 shown schematically in Figs. 8 and 9. In a first preferred embodiment, the tape formation region comprises two cooperating rollers, a grooved roller 60 and a ridged roller 62. Two configurations of the grooved roller 60 and the ridged roller 62 are shown in Figs. 10 and 11a. The ridge of ridged roller 62 cooperates with and fits within the groove of grooved roller 60. The powder fusion coated tow 49 passes between the grooved roller 60 and the ridged roller 62 forming an input powder fusion coated towpreg from tow 49 into a tape 50 of known geometry. Fig. lib shows an alternative configuration of the grooved roller 60 and the ridged roller 62 with the groove being a generally concave configuration and the ridge being generally a convex configuration, the convex configuration cooperating with the concave configuration. As in the rollers 60, 62 shown in Fig. 11a, the convex structure of roller 62 cooperates with and fits within the concave structure of roller 60. The flexible multiply towpreg passes between roller 60 and roller 62 forming an input towpreg from tow 49 into a tape 50 of known geometry. The rollers 60, 62 typically are forced together under a known pressure by an air cylinder 64 mounted on one of the rollers 60, 62, or by any other force-imparting mechanism, such as a spring or hydraulic cylinder. The rollers 60, 62 are placed at the output end of the fusion coating line and correspond to the tape formation region, which substitutes for splitting step 109 shown in Fig. 1. As shown in Fig. 8, the rollers 60, 62 are placed in between the melting step 107, namely the oven 16, and the winding step 116, namely the take-up mechanism 12. In this embodiment, the flexible multiply towpreg exits the oven 16 and the tow 49 temperature is maintained by a heater 66 placed proximate to the rollers 60, 62 at their nip. A suitable heater 66 is a focused quartz infrared lamp, such as that produced by Argus under Model No. 74.285, approximately 2500 watts, controlled by a Stalo energy variac type 3PN1010. Grooved roller 60 is approximately 12.5 cm in diameter and 2.5 cm wide and has a 1.25 cm wide and 0.31 cm deep groove. Ridged roller 62 also is approximately 12.5 cm in diameter and 2.5 cm wide and has a 1.25 cm wide and 0.31 cm high ridge to cooperate with the groove. The rollers, being generally cool, allow the filaments 104 to split, and splitting step 109 often is not necessary. Likewise, cooling step 112 also often is accomplished by the rollers, or by the filaments' 104 exposure to the ambient environment. The tow 49 is pulled through the rollers 60, 62 by take-up mechanism 12. When passing through the rollers 60, 62, one roller is forced against the other roller by the pressure means 64. A suitable pressure means 64 is an air cylinder, such as that produced by Bimba, Model No. 091.5D, with a pressure controller such as the Speedaire 1Z838B regulator. A suitable air cylinder will produce a pressure on the tow 49 of approximately 20 psig for a 0.5 inch wide tow 49. When using a ridged roller 62, the tow 49 is forced into the gap between the rigid and the groove, which is of known geometry, by the ridge and groove geometry of the rollers 60, 62. This geometry causes the tow 49 to come together in the gap and form a flexible tape 50 of the known geometry. The groove of grooved roller 60 and the ridge of rigid roller 62 are selected by the user so as to produce a tape 50 of the desired known geometry. When using a convex roller 62, the tow 49 is forced into the region between the concave structure and the convex structure, causing the tow 49 to be forced together in this region and form a flexible tape 50 also of known geometry. The relative radii of the concave structure of roller 60 and the convex structure of roller 62 are selected by the user so as to produce a tape 50 of the desired known geometry. The rollers 60, 62 typically are cooled with air so as to solidify the matrix material so that the tape 50 can be handled. The tape 50 then passes around guide roller 68 and is wound in take-up mechanism 12. In the embodiment shown in Fig. 9, the roller mechanism replaces the oven 16. When no oven 16 is used, a second heater 70 typically is necessary. A suitable heater is a ceramic heater produced by GTE Sylvania, 500 watts, 12.5 x 6.25 cm, controlled by a Barber-Coleman 560 controller. This heater 70 is used to melt the powder 22 onto the tow 13 to create the powder fusion coated tow 49. The powder fusion coated tow 49 then proceeds through the tape formation region as described above with reference to Fig. 8. The choice of the power densities of the heaters 66, 70 is dependant on the material and the speed of the line. For a 6K carbon fiber tow being coated with PEEK at 1.5 m per minute and being made into a 1.25 cm wide tape, the above described apparatus is suitable. In another embodiment, the tape formation region comprises one crowned or convex roller 60, as shown in Figs. 12 and 13. The powder fusion coated tow 49 is kept under tension as it passes along a portion of the circumference of roller 60. The combination of tension and the concave nature of roller 60 forces the powder fusion coated tow to the lowest point of the concave region forming an input towpreg from tow 49 into a tape 50 of known geometry. The tension can be imparted to the towpreg by the take-up mechanism 12 or other apparatuses not shown. By varying the relative radius of the concave structure of roller 60 and the amount of tension placed on the tow 49, the tow 49 can be forced to come together to a flexible tape 50 of a chosen known geometry. As above, roller 60, may be cooled so as to solidify the matrix material so that the tape 50 can be handled. The tape 50 then passes around guide roller 68 and is wound in take-up mechanism 12. Alternatively, a flat roller or rollers can be used, as long as the tension on the tow is suitable to form the flexible multiply towpreg into a tape. Figs. 20, 21 and 22 are photomicrographs of cross-sections of the towpreg produced by the present invention using glass fiber filaments and a polypropylene matrix material. Fig. 23 are photographs of the tape produced by the present invention using polypropylene matrix material and glass fiber reinforcing filaments. Fig. 23a shows a tape produced from a tow having a line speed of 3 m/min on which the matrix material was melted using a 114 IR lamp. 275 kPa was exerted on the roller. Fig. 23b shows a tape produced from a tow haivng a line speed of 1.4 m/min on which the matrix material was melted at 370°C. 275 kPa was exerted on the roller. The tape from powder fusion coated towpreg disclosed herein has a well-characterized geometry suitable for processes such as filament winding, advanced tow placement, and pultrusion. In filament winding, the tow is wrapped around a mandrel in the shape of a final product. The lay-down head indexes across the mandrel a fixed distance as controlled by an open-loop controller. As an open-loop controller does not measure the width of the material, if the material is too narrow a gap is produced, and if the material is too wide an overlap is produced. Either of these defects can adversely affect the final part's properties. Advanced tow placement has requirements similar to those of filament winding. In pultrusion, fiber bundles are pulled through a die to form a continuous two-dimensional shape. If the input material is not well-characterized geometrically, it will have to realign itself in the die, leading to a poor distribution of fibers in the final part, otherwise the materials and/or the die may fail. This can lead to an increase in pulling force, due, in part, to the friction generated as the fibers reposition themselves, leading to the failure of the fibers or possibly even the die. All of these defects point out the need for a towpreg of known geometry. Additionally, processes such as filament winding and pultrusion require a flexible material as the input to assure high quality final products. The flexible multiply tape resulting from this invention produces flexibility as well as geometric accuracy. c. Non-Woven Fabrics To produce non-woven fabrics, as or after the towpregs 133 are or have been cooled, the towpregs 133, as shown in Figs. 14 - 17, are then arranged, either manually or mechanically, into a desired or proper configuration for producing a desired fabric 139. For example, the towpregs 133 can be arranged unidirectionally as shown in Fig. 14a, multidirectionally as shown in Fig. 15a, or in any directional relationship. The towpregs 133 then are overlayed and joined together to form the non-woven, flexible, multiply towpreg fabric 139 of this invention. Various mechanisms are available for suitably joining the towpregs 133 together. Hot melt bonding of the overlayed towpregs at selected points creates point bonds 137 resulting in a towpreg fabric. Various bonding patterns can be used, with the pattern shown in Fig. 16 shown for example purposes. Alternatively, stitching or weaving with a binder filament or yarn, needle punching, water-jet impingement or pressure point bonding can be used to join the towpregs 133 together. As shown in Fig. 17, stitches 138 result in a suitable fabric 139. Fig. 24 shows a photograph of a non-woven fabric of unidirectional towpregs bound together by interleaving filaments. The towpregs 133 also can be formed into 3-dimensional non-woven fabrics, non-woven fabrics having complex contours, or 2-dimensional or 3-dimensional preforms by using a multiaxial layup mechanism. A take-up mandrel (not shown) can be configured to result in a fabric or preform of any desired configuration. The products of this invention are well-suited for fabricating a variety of composite structures. The fabric can be processed like tacky thermoset prepreg tape to layup advanced composite structures. The fabric can be used to make bonded preforms for resin transfer molding or compression molding. Tubular preforms can be made by tube rolling, a common process for fabricating golf club shafts, tennis rackets, and sailing masts. In addition, a low cost 2-dimensional fabric can be produced for later downstream processing. In this regard, the products of this invention are less expensive than braided or woven fabrics produced from flexible multiply towpreg. Fabrics with matrices, which are solid at room temperature, can be flexible using this technology, whereas conventional technology leads to rigid fabrics. This invention achieves both flexibility and significant fiber wetout using a solid matrix. Fabric structures in which both the matrix and reinforcement are present as fibers, such as commingled, cobundled, or colayered structures, are flexible but do not exhibit any wetting of the reinforcing fibers. Therefore, these cofiber fabrics require more intensive fiber processing conditions to consolidate compared to this invention. The above description has been offered for illustrative purposes only, and is not intended to limit the scope and equivalents of the present invention, which is as defined in the claims below.

Claims: What is claimed is: 1. A method for the production of an improved flexible towpreg comprising a plurality of towpreg plies, said towpreg plies comprising reinforcing filaments and matrix forming material, comprising the steps of: (a) spreading a tow comprising a plurality of reinforcing filaments to expose said reinforcing filaments in a generally columnated manner; (b) coating said reinforcing filaments with said matrix forming material in a manner causing interfacial adhesion of said matrix forming material to said reinforcing filaments; and (c) forming said towpreg plies by liquefying said matrix forming material contacting said reinforcing filaments until said matrix forming material coats said reinforcing filaments. 2. The method as claimed in Claim 1, further comprising the step of: (d) cooling said towpreg plies in a manner such that substantial cohesion between neighboring towpreg plies is prevented until said matrix forming material solidifies. 3. The method as claimed in Claim 2, further comprsing the step of: (e) splitting said coated reinforcing filaments from each other. 4. The method as claimed in Claim 1, further comprising the step of: (d) forming a fusion coated towpreg tape by passing said fusion coated towpreg through a forming means. 5. The method as claimed in Claim 4, wherein said forming means imparts pressure to said fusion coated towpreg. 6. The method as claimed in Claim 5, wherein said step for forming a fusion coated towpreg tape is carried out at a temperature at which said matrix forming material is pliable. 7. The method as claimed in Claim 6 further comprising the step of cooling said towpreg plies in a manner such that substantial cohesion between neighboring towpreg plies is prevented until said fusion coated towpreg is formed into said fusion coated towpreg tape. 8. The method as claimed in Claim 4, wherein said tape forming step is accomplished by means of two or more cooperating rollers, at least one of said rollers having a generally protruding circumferential structure and at least one of said rollers having a generally intruding circumferential structure, said fusion coated towpreg passing between the intruding circumferential structure and the protruding circumferential structure, a force being imparted to at least one of said rollers thereby imparting said force to said fusion coated towpreg as it passes between said roller. 9. The method as claimed in Claim 4, wherein said tape forming step is accomplished by means of a roller having a generally intruding circumferential structure, said fusion coated towpreg being held in tension and within at least a portion of said intruding circumferential structure. 10. The method as claimed in Claim 2, further comprising the steps of: (e) overlapping layers comprising at least one of said towpregs in a manner such that a multilayer configuration of towpregs is formed; and (f) joining said overlapped towpregs together to form a non-woven towpreg fabric. 11. The method as claimed in Claim 10, wherein said layers of towpregs are overlapped in a unidirectional con iguration in step (e) . 12. The method as claimed in Claim 10, wherein said layers of towpregs are overlapped in a multidirectional configuration in step (e) . 13. The method as claimed in Claim 10, wherein said towpregs are joined together using a bonding method selected from the group consisting of hot melt bonding, stitching, needle punching, pressure point bonding, fluid impingement entanglement, binder filament interleaving, and binder yarn interleaving. 14. The method as claimed in Claim 10, wherein steps (e) and (f) are repeated a plurality of times. 15. The method as claimed in Claim 2, further comprising the steps of: (e) overlapping layers comprising at least one of said towpregs in a manner such that a multilayer configuration of towpregs is formed; (f) arranging said towpregs into a desired preform configuration; and (g) bonding said towpregs together so as to form a preform. 16. The method as claimed in Claim 15, wherein steps (e), (f) and (g) are carried out in any order. 17. The method as claimed in Claim 15, wherein any or all of steps (e) , (f) and (g) are carried out simultaneously. 18. The method as claimed in Claim 15, wherein steps (e) , (f) and (g) are repeated a plurality of times. 19. The method as claimed in Claim 2, further comprising the step of: (e) configuring said multiply towpregs into a composite article. 20. The method as claimed in Claims 1, 2, 3, 4, 10, 15, or 18, wherein said matrix forming material further comprises virgin plastic. 21. The method as claimed in Claims 1, 2, 3, 4, 10, 15, or 18, wherein said matrix forming material consists essentially of recycled plastic. 22. The method as claimed in Claims 1, 2, 3, 4, 10, 15, or 18, wherein said matrix forming material is first chopped and then ground to provide a powder prior to coating said reinforcing filaments. 23. The method as claimed in Claim 22, wherein said matrix forming material consists essentially of a blend of virgin and recycled plastics. 24. The method as claimed in Claim 21, wherein said matrix forming material consists essentially of one type of recycled plastic. 25. The method as claimed in Claims 1, 2, 3, 4, 10, 15, or 18, wherein said spreading is lateral. 26. The method as claimed in Claims 1, 2, 3, 4, 10, 15, or 18, wherein said speading of said reinforcing filaments is maintained by axial tension on said reinforcing filaments. 27. The method as claimed in Claims 1, 2, 3, 4, 10, 15, or 18, wherein said matrix forming material is in powder form when contacted with said reinforcing filaments. 28. The method as claimed in Claim 27, wherein said powder comprises particles whose average diameter is greater than twice the average diameter of said reinforcing filaments. 29. The method as claimed in Claims 1, 2, 3, 4, 10, 15, or 18, wherein said matrix forming material is selected from the group consisting of ABS group, acetals, acrylics, alkyd polyesters, allyls, aminos, epoxies, fluoroplastics, furans, melamines,nylons, phenolics, phenylene oxides and ethers, polyamides, polyamide-imides, polybutylenes, polycarbonates, polyesters, polyetheretherketones (PEEK), polyetherketoneketones (PEKK), polyetherketones (PEK), polyetherimides, polyethylenes, polyimides, polymethylpentenes, polyphenylene sulfides, polypropylenes, polystyrenes, polyurethanes, sulfones, ureas and vinyls, and blends thereof, copper, low melting-point metals, and precursor ceramics. 30. The method as claimed in Claims 1, 2, 3, 4, 10, 15, or 18, wherein said filaments have an average diameter no greater than 25 microns. 31. The method as claimed in Claim 30, wherein said filaments are continuous. 32. The method as claimed in Claim 31, wherein said filaments have a melting temperature more than the consolidation temperature of the resulting towpreg. 33. The method as claimed in Claims 1, 2, 3, 4, 10, 15, or 18, wherein said filaments are electrically grounded. 34. The method as claimed in Claims 1, 2, 3, 4, 10, 15, or 18, wherein said filament is selected from the group consisting of glass fibers, carbon fibers, graphite fibers, organic fibers, ceramic fibers, metal fibers, and hybrid fibers. 35. The method as claimed in Claim 34, wherein said organic fiber is selected from the group consisting of liquid crystal fibers that are not low melting. 36. The method as claimed in Claim 35, wherein said hybrid fiber is selected from the group consisting of aramid/carbon, aramid/glass, aramid/carbon/glass, and carbon/glass fibers. 5 37. The method as claimed in Claims 1, 2, 3, 4, 10, 15, or 18, wherein said filaments are split from each other during said cooling step. 38. The method as claimed in Claims 1, 2, 3, 4, 10, 15, or 18, wherein said filaments are split from each 10 other before said cooling step. 39. The method as claimed in Claims 1, 2, 3, 4, 10, 15, or 18, wherein said reinforcing filaments are substantially wetout by said matrix forming material. 40. The method as claimed in Claims 1, 2, 3, 4, 15 10, 15, or 18, wherein said plies have an average length greater than their average width. 41. The method as claimed in Claim 40, wherein said plies have an average width greater than their average thickness. 0 42. The method as claimed in Claim 41, wherein said average length is at least about 30 times said width. 43. The method as claimed in Claims 1, 2 , 3, 4, 10, 15, or 18, wherein the matrix forming material content of said towpreg plies is more than 25% by volume. 5 44. The method as claimed in Claims 1, 2, 3, 4, 10, 15, or 18, wherein said towpreg plies have an average ply thickness of less than about 100 microns. 45. The method as claimed in Claim 44, wherein said towpreg plies have an average ply thickness of less 0 than about 75 microns. 46. The method as claimed in Claim 45, wherein said towpreg plies have an average ply thickness of between about 10 and about 50 microns. 47. The method as claimed in Claim 46, wherein 5 said towpreg plies have an average ply thickness of between about 15 and about 30 microns. 48. The method as claimed in Claims 2, 3, 10, 15, or 18, wherein groups of said coated reinforcing filaments form said towpreg plies during said cooling step (f). 5 49. The method as claimed in Claims 1, 2, 3, 4, 10, 15, or 18, further including a step for desizing said reinforcing filaments between said spreading step and said coating step. 50. The method as claimed in Claims 1, 2, 3, 4, 10 10, 15, or 18, further including a step for applying adhesion promoters or size to said reinforcing filaments between said spreading step and said coating step. 51. The method as claimed in Claims 1, 2, 3, 4, 10, 15, or 18, further including a step for surface 15 activation of said reinforcing filaments between said spreading step and said coating step. 52. The method as claimed in Claims 1, 2, 3, 4, 10, 15, or 18, further comprising a gathering step. 53. The method as claimed in Claims 1, 2, 3, 4, 20 10, 15, or 18, further comprising a polishing step. 54. The method as claimed in Claims 1, 2, 3, 4, 10, 15, or 18, wherein said coating is accomplished by an electrostatic fluidized bed coating means. 55. The method as claimed in Claims 1, 2, 3, 4, 25 10, 15, or 18, wherein said coating is accomplished by a powder spray coating means. 56. An improved flexible towpreg comprising a plurality of towpreg " plies, said towpreg plies comprising reinforcing filaments and matrix forming material; said 0 reinforcing filaments being spread in a generally columnated manner and further being substantially wetout by said matrix forming material such that said towpreg plies are substantially consolidated composite articles, and said towpreg plies having an average thickness less 5 than 100 microns. 57. An improved flexible towpreg tape of a known geometry comprising the towpreg as claimed in Claim 56, wherein said towpreg plies are formed into said towpreg tape such that said towpreg plies have fewer voids than said towpreg tape. 58. The improved flexible towpreg tape as claimed in Claim 57, produced by a process comprising the steps of: (a) providing reinforcing filaments and matrix forming material; (b) coating said reinforcing filaments with said matrix forming material; (c) forming a fusion coated towpreg by heating said reinforcing filaments and said matrix forming material such that said matrix forming material contacting said reinforcing filaments liquifies and coats said reinforcing filaments; and (d) subjecting said fusion coated towpreg to a forming force by passing said fusion coated towpreg through a forming means, thus creating a fusion coated towpreg tape. 59. A non-woven towpreg fabric .comprising a plurality of the towpregs claimed in Claim 56, wherein said towpregs are arranged in overlapping layers comprising at least one towpreg and are joined together resulting in said non-woven towpreg fabric. 60. A multidimensional preform fabricated from the non-woven towpreg fabric as claimed in Claim 59, wherein said towpregs are arranged in overlapping layers comprising at least one towpreg and are joined together in a desired configuration to form said preform. 61. A composite article fabricated from a plurality of the towpregs claimed in Claim 56, wherein said plurality of towpregs are arranged in a desired configuration and joined together resulting in a contoured preform having the general configuration of said composite article, and said preform is further acted upon to form said composite article. 62. A composite article comprising a plurality of the towpregs claimed in Claim 56, wherein said matrix forming material comprises recycled plastic; said reinforcing filaments being substantially wetout by said matrix forming material such that said towpreg plies have a lower void content compared to said multiply towpreg. 63. The improved flexible towpreg as claimed in Claims 56 - 62, wherein said towpreg plies have an average thickness less than 75 microns. 64. The improved flexible towpreg as claimed in Claim 63, wherein said towpreg plies have an average thickness of between about 10 to 50 microns. 65 The improved flexible towpreg as claimed in Claim 64, wherein said towpreg plies have an average thickness of between about 15 to 30 microns. 66. The improved flexible towpreg tape as claimed in Claims 56 - 62, wherein said towpreg plies are connected to neighboring towpreg plies by a common reinforcing filament. 67. The non-woven towpreg fabric as claimed in Claim 59, wherein said layers of towpregs are overlapped in a unidirectional configuration. 68. The non-woven towpreg fabric as claimed in Claim 59, wherein said layers of towpregs are overlapped in a multidirectional configuration. 69. The non-woven towpreg fabric as claimed in Claim 59, wherein said towpregs are joined together using a joining method selected from the group consisting of hot melt bonding, stitching, needle punching, pressure melting 5 of the matrix forming material, pressure point bonding, fluid impingement entanglement, binder filament interleaving, and binder yarn interleaving. 70. The composite article as claimed in Claim 62, wherein said matrix forming material further comprises 10 virgin plastic. 71. The composite article as claimed in Claim 62, wherein said matrix forming material consists essentially of recycled plastic. 72. The composite article as claimed in Claim 15 62, wherein said matrix forming material consists essentially of a blend of plastics. 73. The composite article as claimed in Claim 62, wherein said matrix forming material consists essentially of one type of recycled plastic. 0 74. The articles as claimed in Claims 56-61, wherein said towpreg plies have a lower void content compared to said towpreg.

Inventors: COLTON JONATHAN S, MUZZY JOHN D, VARUGHESE BABU, COLTON, JONATHAN, S., MUZZY, JOHN, D., VARUGHESE, BABU
Applicants: GEORGIA TECH RES INST, GEORGIA TECH RESEARCH CORPORATION
Application year: 1992
Main classification: B32B5
IPC codes: B29B11, B29B15, B29C70, B29K105, C08J5