Factors controlling drug release in cross-linked poly(valerolactone) based matrices
US-2024368351-A1 · Nov 7, 2024 · US
US8952126B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-8952126-B2 |
| Application number | US-201313938874-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 10, 2013 |
| Priority date | Jul 10, 2013 |
| Publication date | Feb 10, 2015 |
| Grant date | Feb 10, 2015 |
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A method of making a pure block copolymer includes forming a crude block copolymer; heating a solution of the crude block copolymer and alcohol; and cooling the solution to promote precipitation of a purified block copolymer, wherein an amount of impurities remaining in the purified block copolymer is from about 0 to about 5 wt % based on a total weight of the purified block copolymer; a ratio of a polydispersity index of the crude block copolymer to a polydispersity index of the purified block copolymer is from about 1.02 to about 1.25; a ratio of a molecular weight of the crude block copolymer to a molecular weight of the purified block copolymer is from about 0.75 to about 1.0; and a ratio of a number average molecular weight of the crude block copolymer to a number average molecular weight of the purified block copolymer is from about 0.65 to about 1.
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What is claimed is: 1. A method of purifying a block copolymer comprising: heating a solution containing a crude block copolymer and an alcohol; cooling the solution to promote precipitation of a purified block copolymer; and isolating the purified block copolymer, wherein isolating the purified block copolymer comprises filtering the solution to separate the purified block copolymer from a filtrate and recovering unreacted monomer and catalyst from the filtrate, and further wherein: an amount of impurities remaining in the purified block copolymer is from about 0 to about 5 wt % based on a total weight of the purified block copolymer; a ratio of a polydispersity index of the crude block copolymer to a polydispersity index of the purified block copolymer is from about 1.02 to about 1.25; a ratio of a molecular weight of the crude block copolymer to a molecular weight of the purified block copolymer is from about 0.75 to about 1.0; and a ratio of a number average molecular weight of the crude block copolymer to a number average molecular weight of the purified block copolymer is from about 0.65 to about 1. 2. The method of claim 1 , wherein the block copolymer is a functionalized block copolymer of a polyester/polycarbonate hybrid. 3. The method of claim 2 , wherein the block copolymer is a polycaprolactone-b-polycarbonate-b-polylactide block copolymer. 4. The method of claim 1 , wherein the alcohol is methanol. 5. The method of claim 1 , wherein the solution is heated to a temperature of from about 50° C. to about 120° C. 6. The method of claim 1 , wherein the solution is cooled to a temperature of from about −30° C. to about 10° C. 7. A method of making a block copolymer comprising: forming a crude block copolymer; heating a solution containing the crude block copolymer and alcohol; cooling the solution to promote precipitation of a purified block copolymer; and isolating the purified block copolymer, wherein isolating the purified block copolymer comprises filtering the solution to separate the purified block copolymer from a filtrate and recovering unreacted monomer and catalyst from the filtrate, and further wherein: an amount of impurities remaining in the purified block copolymer is from about 0 to about 5 wt % based on a total weight of the purified block copolymer; a ratio of a polydispersity index of the crude block copolymer to a polydispersity index of the purified block copolymer is from about 1.02 to about 1.25, a ratio of a molecular weight of the crude block copolymer to a molecular weight of the purified block copolymer is from about 0.75 to about 1.0; and a ratio of a number average molecular weight of the crude block copolymer to a number average molecular weight of the purified block copolymer is from about 0.65 to about 1.0. 8. The method of claim 7 , wherein forming the crude block copolymer comprises a one-pot, organocatalytic, neat ring-opening polymerization. 9. The method of claim 8 further comprising polymerizing the mixture to form a block copolymer, wherein the polymerization comprises: sequentially adding monomers to a reactor to form a mixture; capping the mixture with succinic anhydride; and cooling the mixture to room temperature to form the crude block copolymer. 10. The method of claim 9 , wherein sequentially adding monomers comprises: adding ε-caprolactone, and a catalyst to the reactor to form a first reaction mixture; heating the first reaction mixture; polymerizing a first block; adding a functionalized carbonate monomer to the reactor to form a second reaction mixture; polymerizing a second block; adding D,L-lactide to the reactor to form a third reaction mixture; and polymerizing a third block. 11. The method of claim 7 , wherein the block copolymer is a functionalized block copolymer of a polyester/polycarbonate hybrid. 12. The method of claim 11 , wherein the block copolymer is a polycaprolactone-b-polycarbonate-b-polylactide block copolymer. 13. The method of claim 7 , wherein the alcohol is methanol. 14. The method of claim 7 , wherein the solution is heated to a temperature of from about 50° C. to about 120° C. 15. A one-pot method of making an ABC tri-block copolymer, the method comprising: adding ε-caprolactone, hexanol, and a catalyst to a reactor vessel to form a first reaction mixture; heating the first reaction mixture at a temperature within a range of from about 125° C. to about 145° C. for about 36 to about 72 hours to ring-open and polymerize the ε-caprolactone, forming a reaction mixture comprising an A block polymer; adding a functionalized carbonate monomer to the reaction mixture comprising the A block polymer to form a second reaction mixture; maintaining the second reaction mixture at a temperature within a range of from about 125° C. to about 145° C. for about 20 to about 40 minutes to ring-open and polymerize the functionalized carbonate monomer with the A block, forming a reaction mixture comprising an AB block copolymer; adding D,L-lactide to the reaction mixture comprising the AB block copolymer to form a third reaction mixture; maintaining the third reaction mixture at a temperature within a range of from about 125° C. to about 145° C. for about 20 to about 40 minutes to ring-open and polymerize the D,L-lactide with the AB block copolymer, forming a reaction mixture comprising an ABC tri-block copolymer; adding succinic anhydride to the reaction mixture comprising the ABC tri-block copolymer to form a fourth reaction mixture; maintaining the fourth reaction mixture at a temperature within a range of from about 125° C. to about 145° C. for about 2 to about 12 minutes to cap the ABC tri-block copolymer with the succinic anhydride to form a clear melt comprising a capped ABC tri-block copolymer; cooling the clear melt to room temperature to form a crude solid; adding methanol to the crude solid to form a solution; heating the solution containing the crude solid and methanol to a temperature of from about 130° C. to about 140° C. and refluxing for about 0.1 to about 1 hours; cooling the refluxed solution to a temperature of from about −30° C. to about 10° C. for about 8 to about 20 hours; and isolating a solid from the cooled reflux solution to obtain a purified capped ABC tri-block copolymer; wherein: the purified copolymer is a polycaprolactone-b-polycarbonate-b-polylactide block copolymer; a ratio of a polydispersity index of the crude solid to a polydispersity index of the purified copolymer is from about 1.02 to about 1.25; a ratio of a molecular weight of the crude solid to a molecular weight of the purified block copolymer is from about 0.75 to about 1.0; a ratio of a number average molecular weight of the crude solid to a number average molecular weight of the purified copolymer is from about 0.65 to about 1.0; and an amount of impurities remaining in the purified copolymers is from about 0 to about 5 wt % based on a total weight of the purified copolymer.
derived from hydroxycarboxylic acids · CPC title
Polyesters containing both carboxylic ester groups and carbonate groups · CPC title
Purification; Drying · CPC title
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