Non-curling polyhydroxyalkanoate sutures
First Claim
1. A polymeric filament comprising 4-hydroxybutyrate or copolymers thereof, wherein the filament has an elongation to break from 17% to 85%, a Young'"'"'s modulus of less than 350,000 psi, tenacity to modulus ratio between 0.25 to 1.0, and a load at break between 1100 and 4200 kg, and is produced by extrusion, orientation, relaxation and annealing of the extruded filament.
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Accused Products
Abstract
Absorbable polyester fibers, braids, and surgical meshes with improved handling properties have been developed. These devices are preferably derived from biocompatible copolymers or homopolymers of 4-hydroxybutyrate. These devices provide a wider range of in vivo strength retention properties than are currently available and have a decreased tendency to curl, in the preferred embodiment, due to the inclusion of relaxation and annealing steps following extrusion and orientation of the fiber. Filaments prepared according to these methods are characterized by the following physical properties: (i) elongation to break from about 17% to about 85% (ii) Young'"'"'s modulus of less than 350,000 psi, (iii) knot to straight ratio (knot strength/tensile strength) of 55-80% or (iv) load at break from 1100 to 4200 grams.
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Citations
16 Claims
- 1. A polymeric filament comprising 4-hydroxybutyrate or copolymers thereof, wherein the filament has an elongation to break from 17% to 85%, a Young'"'"'s modulus of less than 350,000 psi, tenacity to modulus ratio between 0.25 to 1.0, and a load at break between 1100 and 4200 kg, and is produced by extrusion, orientation, relaxation and annealing of the extruded filament.
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9. A method of making a polyhydroxyalkanoate filament comprising
a) drying the water content of polyhydroxyalkanoate pellets to less than 0.01% (w/w); -
b) feeding the dried polyhyroxyalkanoate pellets into an extruder barrel under a blanket of nitrogen to melt the polyhydroxyalkanoate;
c) passing the molten polyhydroxyalkanoate through a heated block to a metering pump;
d) extruding the polyhydroxyalkanoate from a die with a single hole spinneret to produce a spun extrudate filament;
e) drawing the spun extrudate filament into a heat zone, maintained at a temperature above the melting temperature of the filament, to orient and relax the filament. - View Dependent Claims (10, 11, 12, 13, 14, 15, 16)
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Specification