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A process of producing a fibre-reinforced composition comprising drawing a plurality of continuous filaments through a melt comprising a mixture of a thermoplastic polymer and a plasticizer for the polymer in the weight ratio between 1:4 and 99:1 of polymer to plasticizer, preferably in the weight r

A process of producing a fibre-reinforced composition comprising drawing a plurality of continuous filaments through a melt comprising a mixture of a thermoplastic polymer and a plasticizer for the polymer in the weight ratio between 1:4 and 99:1 of polymer to plasticizer, preferably in the weight ratio 1:1 to 19:1, the plasticizer being thermally stable at least up to the temperature of the melt and having volatility characteristics such that the plasticizer can be volatilized from the composition below the decomposition temperature of the composition but has a sufficiently low volatility at the temperature of the melt to plasticize the polymer in the melt and give a melt of reduced viscosity compared with the melt viscosity of the polymer alone. The process enables higher molecular polymers to be used in the pultrusion process and enables higher fibre contents to be achieved.

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1. A process of producing a fibre-reinforced composition comprising wetting a plurality of continuous filaments with a melt by drawing the filament through a melt which comprises a mixture of a thermoplastic polymer and a plasticiser for the polymer in the weight ratio between 1:4 and 99:1 of polyme

1. A process of producing a fibre-reinforced composition comprising wetting a plurality of continuous filaments with a melt by drawing the filament through a melt which comprises a mixture of a thermoplastic polymer and a plasticiser for the polymer in the weight ratio between 1:4 and 99:1 of polymer to plasticiser the plasticiser being thermally stable at least up to the temperature of the melt and having volatility characteristics such that the plasticiser can be volatilized from the composition below the decomposition temperature of the thermoplastic polymer but has a sufficiently low volatility at the temperature of the melt to plasticise the polymer in the melt and give a melt of reduced viscosity compared with the melt viscosity of the polymer alone, and substantially reducing the plasticiser content of the composition while the wetted filaments are at a temperature above the glass transition temperature of the polymer alone but below the decomposition temperature of the polymer such that the plasticiser content is 5% or less by weight of the composition. 2. A process according to claim 1 wherein the melt viscosity of the polymer in the absence of the plasticiser is at least 100 Ns/m 2 at zero shear rate measured below the decomposition temperature of the polymer. 3. A process according to either of claim 1 or claim 2 in which the polymer/plasticiser melt is contained within a melt bath provided with at least one spreader surface over which the plurality of filaments are pulled. 4. A process according to claim 1 or claim 2 in which the impregnated plurality of fibres is spread into a thin band of contiguous filaments by biassing the plurality of fibres against at least one spreader surface and supplying sufficient heat to the band to produce a fibre reinforced structure substantially free of plasticiser. 5. A process according to either of claims 1 or 2 in which contiguous filaments which are pulled over a spreader surface to form a nip between the band and the spreader surface and a molten mixture of polymer and plasticiser is provided at the nip, impregnation of the band formed by the contiguous filaments being effected by tensioning the continuous band so that positive pressure is applied on the polymer melt by the band as it is pulled over the spreader surface. 6. A process according to claim 5 in which the polymer melt is maintained in a molten state during impregnation by supplying at least part of the heat required to at least one spreader surface. 7. A process according to claim 5 in which the polymer melt is maintained in a molten state during impregnation by supplying at least part of the heat required directly to the filaments. 8. A process according to claim 1 or claim 2 in which the thermoplastic polymer is an aromatic polymer and comprises a polymer of repeat unit of the general formula: ##EQU##--Ar--X-- where Ar is selected from mono or polycyclic aromatic radicals and X is selected from at least one of O, S, SO 2, O.CO, O.CO.O, CO, --NHCO-- and ##STR## 9. A process according to claim 8 in which the aromatic polymer is selected from polysulphones, polyethersulphones, polyetherketones, polyetheretherketones, polyarylene oxides, polyarylene sulphides, aromatic polyamides, aromatic polyesters, aromatic polycarbonates, and aromatic polyetherimides. 10. A process according to claim 1 or claim 2 in which the polymer is a polyetherketone or polyetheretherketone and the plasticiser is an aromatic sulphone. 11. A fibre-reinforced structure produced by the process of claim 1 or claim 2 or claim 12 and having a plasticiser content of between 0.1 and 5% by weight of the structure. 12. A process according to claim 1 wherein the fibre-reinforced composition has at least 50% by volume of reinforcing fibres. 13. A process according to claim 1 wherein any residual plasticiser in the composition is a solid at ambient temperature.