Process for purifying resorbable polyesters

Claim 2

A process for the purification of polymers, characterized in that the polymer is dissolved in a solvent and the polymer solution is subsequently brought into intimate contact with a precipitation agent under the effect of high shear forces in a turbulent shear field, so that the polymer precipitated is divided up into minute particles.

Claim 3

The process as claimed in claim 1, further characterized in that the polymer to be purified is a resorbable polyester which is a polymer or copolymer based on L-lactide, D-lactide, D,L-lactide, meso-lactide, glycolide and/or caprolactone.

Claim 4

The process as claimed in claim 2, further characterized in that the crystallinity of the polyester is between zero and 70%.

Claim 5

The process as claimed in claim 3, further characterized in that the crystallinity of the polyester is between zero and 20%.

Claim 6

The process as claimed in claim 1, further characterized in that the precipitation agent is an organic solvent.

Claim 7

The process as claimed in claim 1, further characterized in that the precipitation agent is water.

Claim 8

The process as claimed in claim 1, further characterized in that the precipitation agent consists of a mixture of several solvents.

Claim 9

The process as claimed in claim 1, further characterized in that the precipitation agent consists of a mixture of several solvents and water.

Claim 10

The process as claimed in claim 1, further characterized in that a complexing agent, an acid or a base or an adjuvant for altering the surface tension is added to the precipitation agent.

Claim 11

The process as claimed in claim 1, further characterized in that the solvent is acetone, dimethylacetamide, dioxan, tetrahydrofuran, dimethylformamide or dimethyl-sulphoxide and the precipitation agent is water.

Claim 12

The process as claimed in claim 1, further characterized in that the solvent is chloroform or methylene chloride and the precipitation agent is hexane, petroleum ether or a freon.

Claim 13

The process as claimed in claim 1, further characterized in that the temperature of the polymer solution or the precipitation agent or both is between ambient temperature and the boiling temperature of the solvent or precipitation agent.

Claim 14

The process as claimed in claim 1, further characterized in that the temperature of the polymer solution or precipitation agent or both is between ambient temperature and -20° Celsius.

Claim 15

The process as claimed in claim 1, further characterized in that the turbulent shear field is produced by an apparatus comprising of a stator and a rotor moving relative to this stator.

Claim 16

The process as claimed in claim 14, further characterized in that the polymer solution is metered into the inlet to the apparatus in such as a way that, immediately after being fed in, the polymer solution is introduced into the shear field generated by the rotor and stator.

Claim 17

The process as claimed in claim 1, further characterized in that the turbulent shear field is produced by an apparatus comprising of a two component nozzle and a container filled with precipitation agent into which the two component nozzle projects.

Claim 18

The process as claimed in claim 16, further characterized in that the polymer solution is forced through the narrow inner bore and the precipitation agent is forced through the outer annular channel of the nozzle.

Claim 19

The process as claimed in claims 14 or 16, further characterized in that the polymer precipitated is continuously separated from the precipitation agent with the aid of a centrifuge.

Claim 20

The process as claimed in claims 14 or 16, further characterized in that the polymer precipitated is continuously separated from the precipitation agent with the aid of a pressure suction filter.

Claim 21

The process as claimed in claims 14 or 16, further characterized in that the polymer precipitated is continuously separated from the precipitation agent with the aid of a belt filter.

Claim 22

The process as claimed in claim 1, further characterized in that the polymer to be purified is a resorbable polyester selected from the group comprising the homopolymers and copolymers based on hydroxycarboxylic acids, and polymers based on trioxanone (1,3 and 1,4), dioxanone (1,3 and 1,4), substituted dioxanone, trimethylene carbonate, ethylene carbonate and propylene carbonate and optionally contains as comonomer one or more compounds selected from the group comprising lactic acid, glycolic acid, pentaerythritol, sorbitol, adonitol, xylitol, fructose, epichlorohydrin, isopropylmorpholine, isopropylmethylmorpholinedione, beta-propiolic acid, tetramethylglycolide, beta-butyrolactone, gamma-butyrolactone, pivalolactone, alpha-hydroxybutryic acid, alpha-hydroxyisobutyric acid, alpha-hydroxyisovaleric acid, alpha-hydroxycaproic acid, alpha-hydroxyisocaproic acid, alpha-hydroxy-alpha-ethylbutyric acid, alpha-hydroxy-alpha-methylvaleric acid, alpha-hydroxyheptanoic acid, alpha-hydroxyoctanoic acid, alpha-hydroxydecanoic acid, alpha-hydroxytetradecanoic acid, alph-hydroxystearic acid and alpha-hydroxyvaleric acid.

Claim 23

The process as claimed in claim 21, further characterized in that the resorbable polyester is and copolymers based on glycolide, lactide, methylglycolide, dimethylglycolide, polymethylglycolide, diethylglycolide, dibutylglycolide, caprolactone, valerolactone, decalactone, propiolactone, butyrolactone and pivalolactone.

Claim 24

The process as claimed in claim 21, further characterized in that the resorbable polyester is selected from the group of a copolymer of D,L-lactide and glycolide with inherent viscosities of at least 2.5 dl/g, corresponding to average molecular weights of at least 110,000, a copolymer of e-caprolactone with L-, D,L-lactide and glycolide and inherent viscosities of up to at least 4 dl/g; poly(L-lactide-co-D,L-lactide) in the ratio 9:1, poly(L-lactide-co-glycolide) in the ratio 7:3, poly(D,L-lactide-co-glycolide) in the ratio 3:1, poly(D,L-lactide-co-glycolide) in the ratio 1:1 and poly(D,L-lactide-co-glycolide) in the ratio 45:55.