Process for preparing a bio-resorbable polyester in particulate form

1. A process for preparing a bio-resorbable polyester in particulate form, said process comprising:

a) providing a bio-resorbable polyester in the form of a dry polymer mass or in the form of a wet polymer mass,

b) feeding the polymer mass from a) into an extruder with at least one degassing zone where the polymer mass is molten, extruded and degassed, to obtain a degassed polymer,

c) discharging the degassed polymer mass out of the extruder, and

d) comminuting the discharged polymer mass to particles with

a bulk density of 0.3 g/ml or more,

a tapped density of 0.4 g/ml or more, and

a specific surface area of 2.0 m 2 /g or less.

2. The process according to claim 1 , wherein in a), the bio-resorbable polyester is provided as dry polymer mass in the form of a powder or a granulate with

a bulk density of less than 0.3 g/ml,

a tapped density of less than 0.4 g/ml, and

a specific surface area of more than 2.0 m 2 /g.

3. The process according to claim 1 , wherein in a), the bio-resorbable polyester is provided in the form of a wet polymer mass,

wherein a bioresorbable polyester is dissolved in a first solvent or solvent mixture, and

wherein the polymer solution is then contacted with a second solvent or solvent mixture which is a non-solvent for the bioresorbable polyester and which comprises at least 95% by weight of water to result the precipitation of the bio-resorbable polyester in the form of a wet polymer mass.

4. The process according to claim 3 , whereby in c), the water of the wet polymer mass is removed in the one or more degassing zones of the extruder to result in a degassed polymer mass with water content of 1% or less by weight/weight.

5. The process according to claim 1 , wherein the particles are a powder having a particle size of d 50 of 1-300 μm and d 90 of more than 30 and up to 3000 μm.

6. The process according to claim 1 , wherein the polymer mass in c) is extruded at a melt temperature of the polymer melt in the range of about 80 to 170° C.

7. The process according to claim 1 , wherein the pressure in the degassing zone of the extruder is a vacuum of minus 100 to minus 900 mbar.

8. The process according to claim 1 , wherein the extruder is a double screw extruder.

9. The process according to claim 1 , wherein the mass throughput of the extruded polymer mass through the extruder is from about 0.1 to 10 kg/h.

10. The process according to claim 1 , wherein the bio-resorbable polyester is a polylactic acid, a polyglycolic acid, a poly-caprolactone, a lactic acid-glycolic acid copolymer, a lactic acid-glycolic acid-polyethylene block copolymer, a lactic acid-glycolic acid-caprolactone terpolymer, a lactic acid-caprolactone copolymer, a poly dioxanone, a lactic acid-trimethylene carbonate copolymer or a mixture thereof.

11. The process according to claim 1 , wherein the bio-resorbable polyester is a poly(D,L-lactide-co-glycolide) copolymer with an inherent viscosity from 0.1-2.0.

12. The process according to claim 11 , wherein the proportion of D,L-lactide to glycolide in the poly(D,L-lactide-co-glycolide) copolymer is from 70:30 to 30:70 parts by weight.

13. A bio-resorbable polyester obtainable from a process according to claim 1 , which is in the form of a powder with

a mean particle size d 50 of 1-300 μm,

d 90 of more than 30 and up to 1000 μm,

a bulk density of less 0.3 g/ml or more,

a tapped density of 0.4 g/ml or more, and

a specific surface area of 2.0 m 2 /g or less.

14. A bio-resorbable pharmaceutical active ingredient, comprising:

the bio-resorbable polyester according to claim 13 ,

a dosage form suitable for an in-situ sustained release application in the human body or in an animal body.

15. A bio-resorbable surgical article, comprising:

the bio-resorbable polyester according to claim 13 .

16. The bio-resorbable surgical article according to claim 15 , which is a filament, a rod, a stent or a prostheses.