Method of producing fibre-reinforced composition
AssigneeImperial Chemical Industries PLC
InventorsFrederic N. Cogswell, Philip A. Staniland
Life of this patent
Estimating the term…
Loading patent…
AssigneeImperial Chemical Industries PLC
InventorsFrederic N. Cogswell, Philip A. Staniland
Estimating the term…
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.
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.
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.
Dependencies are inferred from the claim text.