THERMOPLASTIC PULTRUSION

Abstract: A method is provided for producing continuous composite extrusions of thermoplastics material containing continuous bunched strands of fibre reinforcement (1) in which the fibre reinforcement is impregnated with a melted thermoplastics material of relatively low viscosity, such as glycol-modified PET, before being co-extruded with a melted thermoplastics material having a relatively high viscosity, such as PVC, the advantage being that continuous fibre reinforced extrusions (9) can be produced in which the polymer of relatively low viscosity acts as an interface between the reinforcing fibre and the polymer of relatively high viscosity, thereby improving bonding therebetween.

Description: THERMOPLASTIC PULTRUSION This invention relates to composites of plastics having fibre reinforcement therein, such as structural plastics composites in which the fibre is comprised of glass fibre, although it will be understood that other fibres may be used. Hereafter a "strand" of fibre may include multifilaments of such fibre. It is known to manufacture plastics composites by a method known as pultrusion in which glass fibre strands are drawn or pulled through a resin or plastics mixture and subsequently through a die having a required profile, to be then cured or cooled to form a reinforced composite structure. This process has a number of disadvantages, one being the time taken for curing or cooling which may typically be one to three minutes for the latter. Another is that the surface finish of the composite is not particularly smooth because of the presence of the fibres at the surface. In addition, because pultrusion requires the fibres to be bunched together over the whole of the cross-sectional area of the profile corresponding to the die it will be apparent that the composite structure is effectively reinforced with the glass fibre throughout the whole of its cross-section even though structural considerations may not require this. It is known to produce structural composites by means of feeding pre-pultruded and cured or cooled lengths of reinforcing rods or strips through central portions of a conventional extrusion die whilst extruding thermoplastic material such as PVC therearound. This produces a composite structural member having a superior surface finish to that of a conventionally pultruded member whilst benefiting from the increased strength imparted by the interior reinforcement. However, a disadvantage is that the process is not continuous and difficulties can be encountered at the interface between the surface of the pultrusion and the PVC so that they may not be satisfactorily joined together. The present invention is derived from the realisation that although high grade extrusion polymers such as PVC are generally too viscous to be joined directly with reinforcement fibres such as glass fibres when being extruded, nevertheless this problem can be solved by the use of an intermediate low viscosity polymer which is able to impregnate the fibres sufficient to cause them to bond together whilst at the same time allowing the resultant bunched strip to bond with a melted thermoplastics material of relatively high viscosity to thereafter produce extrusions having smooth surface finishes whilst incorporating fibre reinforcement in a continuous process. According to the invention there is provided a method of producing continuous composite extrusions of thermoplastics material containing continuous bunched strands of fibre reinforcement, the method comprising the steps of providing a thermoplastics material having a relatively high viscosity when melted, providing a polymer of relatively low viscosity when melted and subsequently using that melted polymer to impregnate strands of the fibre reinforcement to form an impregnated bunched strip, extruding melted thermoplastics material through an extrusion die and during extrusion feeding the impregnated strip through the die to form a continuous composite with the thermoplastics material, and thereafter cooling the composite extrusion. Conveniently, the thermoplastics material of relatively high viscosity is polyvinyl chloride (PVC) and the polymer of relatively low viscosity is glycol-modified polyethylene terephthalate (PET) , although other suitable polymers may be used including injection-moulding grade ABS, grafted polypropylene and thermoplastic polyurethane, with varying degrees of success. Where the thermoplastics material of relatively high viscosity is polypropylene it has been found that a suitable impregnation polymer is an injection moulding grade of polypropylene i.e. one with relatively low viscosity such as one with a reduced molecular weight relative to conventional polypropylene. In a first embodiment of the method of the invention strands of impregnation polymer are intermingled with strands of glass fibres and then passed through an infrared pre-heater to melt the polymer sufficient to permit impregnation of the glass strands, whereafter the strands are caused to pass through a series of staggered pins or rollers to cause the fibres to intermingle fully with the melted impregnation polymer. Following this step the impregnated glass fibres are passed through consolidation plates to remove trapped air and excess polymer to form an impregnated bunched strip which may then be fed directly into an extrusion die during the otherwise conventional extrusion of the melted thermoplastics material. This may typically be performed by the use of a crosshead die where the melted high viscosity thermoplastic is fed around the impregnated bunched strip, or strips if there are more than one, prior to extrusion through the die. Following such extrusion the composite is then cooled and hauled off in a conventional manner. In a second embodiment of the method of the invention the impregnation process occurs following pre-heating of reinforcement fibres after they have been drawn off from respective fibre creels, with heated polymer being separately provided from a crosshead extruder, although it will be understood that any other method of introducing polymer to the reinforcement fibre strands for impregnation thereof may be used including polymers in powder form, in solution or emulsion. The invention will now be described, by way of example only, with reference to the accompanying drawings in which: Figure 1 shows in schematic form a production line for forming a continuous thermoplastics reinforced composite in accordance with the invention, and Figure 2 shows in cross section a structural member in the form of a roofing beam in si tu and supporting a pair of oppositely disposed roofing sheets, only part of which are shown. In Figure 1 a number of individual strands or rovings (1) of glass fibre are shown being unwound from their respective creels (not shown) through a spacer bar (2) and thereafter bunched together in a generally flat strip before entering into an elongated hollow heating station (3) where the strands are heated by means of an infra-red pre-heater (not shown) up to approximately 200°C prior to exit therefrom. The heated glass fibre strands then pass through a polymer impregnation unit (4) comprising a set of staggered pins shown generally at (5) arranged substantially transverse to the longitudinal direction of travel of the fibres (1) so that they are collectively forced to bend slightly around each of the set of pins (5) . During this process melted impregnation polymer is fed onto the pins in the direction shown arrowed from a small extruder (6) so that as the strip of fibres (1) negotiate the set of pins (5) they collectively become impregnated with the relatively low viscosity polymer prior to exit from the impregnation unit (4). On exiting the impregnation unit (4) the impregnated strip (la) then enters into a cross-head extrusion die (7) which is provided with melted thermoplastics material of relatively high viscosity, such as PVC, via a main extruder (8) with guides (not shown) ensuring that the impregnated strip (la) is retained centrally in position within the die (7) whilst extruded thermoplastics material flows completely around it. The composite extrusion (9) then emerges from the extrusion die (7) to enter a conventional cooling and shaping unit (10) followed by "haul off" in a conventional manner via haul off unit (11) . Following haul off, the extruded composite therefore has a high quality surface finish by virtue of the use of, typically, PVC as the bulk thermoplastics material but includes in the interior one or more localised areas of stiffening as a result of the presence of the bunched fibre reinforcement. Such reinforcement adheres well to the PVC through the intermediary of the impregnation polymer, without which the fibres would not adhere so well to the PVC in view of the relatively high viscosity thereof when melted. It will be apparent from the foregoing that the invention may also be used to make hollow extrusions, such as extrusions used in the building industry. It may, for example, be used to manufacture roofing bars for conservatories, which would otherwise typically be manufactured from extruded aluminium in order to meet stiffness criteria and thereafter be covered with one or more plastics strips or covers in order to provide adequate heat insulation. In Figure 2 there is shown in cross section a composite extrusion made in accordance with the method of the invention in the form of a roofing bar shown generally at 10 for supporting roofing panels 11,12 which may typically be of toughened glass or a transparent plastics material. The beam 10 is secured in place on a bracket (not shown) by bolts 13,14 and is of generally conventional inverted "T"-shaped section having at its upper end a flanged slot 15 for receiving a correspondingly shaped bead portion of a generally "V"-shaped finishing cap (not shown) for securing the panels 11,12 in position. The roofing bar 10 is primarily made from extruded PVC but includes localised areas of stiffening 16,17, each being composed of bunched strands of fibre reinforcement, such as glass fibre reinforcement, bonded together by a polymer of relatively low viscosity such as glycol-modified PET and subsequently co-extruded through a suitably shaped die with the PVC such that upon the composite extrusion being hauled off and subsequently cooled it may be cut up into suitable lengths. In this instance, the localised stiffening provided by the bunched strips 16,17, provides sufficient rigidity to the beam 10 for it to be used to support the roof of, typically, a conservatory in substitution for a correspondingly shaped beam made of aluminium. This has the advantage in that the beam 10 is thermally very efficient and because a high grade polymer such as PVC can be used, an attractive finish can be achieved. In contrast, a correspondingly shaped roofing bar made of extruded aluminium would normally require capping of plastics material in order to provide sufficient heat insulation and, where necessary, a suitably attractive finish. The invention therefore also extends to a composite structural member comprising an extrusion of relatively high viscosity thermoplastics material such as PVC including one or more localised areas of stiffening provided by fibre strands, such as glass fibre strands, embedded within a polymer of relatively low viscosity compared to that of the thermoplastics material, such as glycol-modified PET or, where the thermoplastic is polypropylene, by the use of injection-moulding grade ABS, grafted polypropylene and thermoplastic polyurethane, made in accordance with the methods of the invention.

Claims: CLAIMS 1. A method of producing continuous composite extrusions of thermoplastics material containing continuous bunched strands of fibre reinforcement, the method comprising the steps of providing a thermoplastics material having a relatively high viscosity when melted, providing a polymer of relatively low viscosity when melted and subsequently using that melted polymer to impregnate strands of the fibre reinforcement to form an impregnated bunched strip, extruding the melted thermoplastics material of relatively high viscosity through an extrusion die and during extrusion feeding the impregnated strip through the die to form a continuous composite with the thermoplastics material of relatively high viscosity, and thereafter cooling the composite extrusion. 2. A method according to Claim 1 further characterised in that the thermoplastics material of relatively high viscosity is PVC and the polymer of relatively low viscosity is glycol-modified PET. 3. A method according to Claim 1 or Claim 2 further characterised by including the steps of pre-heating the reinforcement fibres to a temperature approximating the melt temperature of the polymer of relatively low viscosity when melted and thereafter impregnating said fibres with the melted low viscosity polymer to form bunched strands of fibre impregnated with said low viscosity polymer, and thereafter co-extruding said impregnated strands with a polymer of relatively high viscosity to produce a continuous composite extrusion of thermoplastics material containing continuous bunched strands of fibre reinforcement . 4. A method according to Claim 1 or Claim 2 further characterised in that the impregnation polymer is initially in strand form and is then intermingled with the strands of fibre reinforcement to thereafter be melted therearound to form an impregnated bunch of fibres, following which said bunch is co-extruded with a polymer of relatively high viscosity to form a composite extrusion. 5. A composite structural member made in accordance with the method of any preceding Claim. 6. A composite structural member substantially as hereinbefore described with reference to Figure 2. 7. A method of producing a continuous composite extrusion of thermoplastics material containing continuous bunched strands of fibre reinforcement substantially as hereinbefore described with reference to Figure 1.

Inventors: BETTERIDGE JOHN REGINALD, BISHOP GORDON ROLAND, BETTERIDGE, JOHN, REGINALD, BISHOP, GORDON, ROLAND
Applicants: BETTERIDGE JOHN REGINALD, BISHOP GORDON ROLAND, FIBREPLAS EXTRUSIONS LTD, BETTERIDGE, JOHN, REGINALD, BISHOP, GORDON, ROLAND, FIBREPLAS EXTRUSIONS LIMITED
Application year: 2000
Main classification: B29C70
IPC codes: B29B15, B29C47, B29C70