Process for producing a lactic acid-glycolic acid copolymer or a salt thereof

US10011681B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-10011681-B2
Application numberUS-201414782145-A
CountryUS
Kind codeB2
Filing dateApr 8, 2014
Priority dateApr 11, 2013
Publication dateJul 3, 2018
Grant dateJul 3, 2018

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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  7. Citations and related patents

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Abstract

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Provided is a purified lactic acid-glycolic acid copolymer, preferably in the form of powder, having a reduced content of dimers such as residual lactide and glycolide that can be produced by a simple industrial process without the use of any high-shear special device. Further provided is a high-purity lactic acid-glycolic acid copolymer which has small amounts of dimers such as residual lactide and glycolide and small amounts of a low-molecular weight lactic acid-glycolic acid copolymer or a salt thereof and which has a small ratio of weight average molecular weight to number average molecular weight (Mw/Mn). The copolymer can be produced in accordance with a defined process.

First claim

Opening claim text (preview).

The invention claimed is: 1. A process for producing a purified lactic acid-glycolic acid copolymer (A2) or a salt thereof comprising the steps of: (1-1) dissolving a lactic acid-glycolic acid copolymer (A1) containing lactic acid units and glycolic acid units or a salt thereof into at least one organic solvent (B1) having a solubility at 25° C. of not less than 1 wt % to prepare a solution of the lactic acid-glycolic acid copolymer (A1) or the salt thereof; (1-2) adding at least one solvent (S1) selected from water and aliphatic alcohols (B2) to the solution of the lactic acid-glycolic acid copolymer (A1) or the salt thereof to prepare a second solution including the lactic acid-glycolic acid copolymer (A1) or the salt thereof, the organic solvent (B1) and the at least one solvent (S1); (2) adding the second solution prepared in the step (1-2) to a solvent (S2′) including at least one selected from water and aliphatic alcohols (B2) to precipitate a purified lactic acid-glycolic acid copolymer (A2) or a salt thereof; and (3) recovering the precipitate of the purified lactic acid-glycolic acid copolymer (A2) or the salt thereof. 2. The process for producing a purified lactic acid-glycolic acid copolymer (A2) or a salt thereof according to claim 1 , wherein the lactic acid-glycolic acid copolymer (A1) contains 40 to 90 mol % of the lactic acid units and 60 to 10 mol % of the glycolic acid units (wherein the total of the lactic acid units and the glycolic acid units is 100 mol %). 3. The process for producing a purified lactic acid-glycolic acid copolymer (A2) or a salt thereof according to claim 1 , wherein the lactic acid-glycolic acid copolymer (A1) has a weight average molecular weight (Mw) in the range of 4,500 to 110,000. 4. The process for producing a purified lactic acid-glycolic acid copolymer (A2) or a salt thereof according to claim 1 , wherein in the step (1-1), the lactic acid-glycolic acid copolymer (A1) or the salt thereof is dissolved into the organic solvent (B1) with a concentration of 1 to 50 wt %. 5. The process for producing a purified lactic acid-glycolic acid copolymer (A2) or a salt thereof according to claim 1 , wherein the organic solvent (B1) used in the step (1-1) is an aprotic polar organic solvent. 6. The process for producing a purified lactic acid-glycolic acid copolymer (A2) or a salt thereof according to claim 1 , wherein the addition in the step (2) is dropwise addition. 7. The process for producing a purified lactic acid-glycolic acid copolymer (A2) or a salt thereof according to claim 1 , wherein in the step (2), the purified lactic acid-glycolic acid copolymer (A2) or the salt thereof is precipitated as a powder. 8. The process for producing a purified lactic acid-glycolic acid copolymer (A2) or a salt thereof according to claim 1 , wherein the process comprises the steps of: (1-1) dissolving a lactic acid-glycolic acid copolymer (A1) or a salt thereof into at least one organic solvent (B1) having a solubility at 25° C. of not less than 1 wt % to prepare a 1-50 wt % solution of the lactic acid-glycolic acid copolymer (A1) or the salt thereof, the lactic acid-glycolic acid copolymer (A1) containing 40 to 90 mol % of lactic acid units and 60 to 10 mol % of glycolic acid units (wherein the total of the lactic acid units and the glycolic acid units is 100 mol %) and having a weight average molecular weight (Mw) in the range of 4,500 to 110,000; (1-2-A) adding at least one solvent (S1) selected from water and aliphatic alcohols (B2) to the solution of the lactic acid-glycolic acid copolymer (A1) or the salt thereof to prepare a second solution including the lactic acid-glycolic acid copolymer (A1) or the salt thereof, the organic solvent (B1) and the at least one solvent (S1); (2) adding dropwise the second solution prepared in the step (1-2-A) to at least one solvent (S2) selected from water and aliphatic alcohols (B2) to precipitate a purified lactic acid-glycolic acid copolymer (A2) or a salt thereof as a powder; and (3) recovering the precipitate of the purified lactic acid-glycolic acid copolymer (A2) or the salt thereof. 9. The process for producing a purified lactic acid-glycolic acid copolymer (A2) or a salt thereof according to claim 1 , wherein the amount of the solvent (S1) used in the step (1-2) is 0.05 to 2.5 times by weight the amount of the organic solvent (B1). 10. The process for producing a purified lactic acid-glycolic acid copolymer (A2) or a salt thereof according to claim 1 , wherein the temperature of the solvent (S2′) used in the step (2) is from the solidification point of the solvent (S2′) to 25° C. 11. The process for producing a purified lactic acid-glycolic acid copolymer (A2) or a salt thereof according to claim 1 , wherein the amount of the solvent (S2′) used in the step (2) is 3 or more times by weight the amount of the organic solvent (B1). 12. A process for producing a purified lactic acid-glycolic acid copolymer (A2) or a salt thereof comprising the steps of: (1-1) dissolving a lactic acid-glycolic acid copolymer (A1) containing lactic acid units and glycolic acid units or a salt thereof into at least one organic solvent (B1) having a solubility at 25° C. of not less than 1 wt % to prepare a solution of the lactic acid-glycolic acid copolymer (A1) or the salt thereof; (1-2-B1) adding at least one solvent (B2) selected from water and aliphatic alcohols to the solution of the lactic acid-glycolic acid copolymer (A1) or the salt thereof and stirring the mixture to separate the mixture into two liquid phases; and (1-2-B2) recovering one of the two phases which includes the lactic acid-glycolic acid copolymer or the salt thereof having a larger weight average molecular weight (Mw) (2) adding the phase recovered in the step (1-2-B2) to a solvent including at least one selected from water and aliphatic alcohols to precipitate a purified lactic acid-glycolic acid (A2) or a salt thereof; and (3) recovering the precipitate of the purified lactic acid-glycolic acid copolymer (A2) or the salt thereof. 13. The process for producing a purified lactic acid-glycolic acid copolymer (A2) or a salt thereof according to claim 12 , wherein the process comprises the steps of: (1-1) dissolving a lactic acid-glycolic acid copolymer (A1) or a salt thereof into at least one organic solvent (B1) having a solubility at 25° C. of not less than 10 wt % to prepare a 10-50 wt % solution of the lactic acid-glycolic acid copolymer (A1) or the salt thereof, the lactic acid-glycolic acid copolymer (A1) containing 40 to 90 mol % of lactic acid units and 60 to 10 mol % of glycolic acid units (wherein the total of the lactic acid units and the glycolic acid units is 100 mol %) and having a weight average molecular weight (Mw) in the range of 4,500 to 105,000; (1-2-B1) adding at least one aliphatic alcohol (B2) to the solution of the lactic acid-glycolic acid copolymer (A1) or the salt thereof and stirring the mixture to separate the mixture into two liquid phases; (1-2-B2) recovering one of the two phases which includes the lactic acid-glycolic acid copolymer or the salt thereof having a larger weight average molecular weight (Mw); (2) adding dropwise the phase recovered in the step (1-2-B2) to a solvent including water to precipitate a purified lactic acid-glycolic acid (A2) or a salt thereof; and (3) recovering the precipitate of the purified lactic acid-glycolic acid copolymer (A2) or the salt thereof. 14. The process for producing a purified lactic acid-glycolic acid copolymer (A2) or a salt thereof according to claim 13 , wherein the solvent to which the recovered phase is added dropwise in the ste

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Inventors

Classifications

  • Macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds, e.g. polyesters, polyamino acids, polysiloxanes, polyphosphazines, copolymers of polyalkylene glycol or poloxamers (A61K47/10 takes precedence) · CPC title

  • C08G63/90Primary

    Purification; Drying · CPC title

  • derived from hydroxycarboxylic acids · CPC title

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What does patent US10011681B2 cover?
Provided is a purified lactic acid-glycolic acid copolymer, preferably in the form of powder, having a reduced content of dimers such as residual lactide and glycolide that can be produced by a simple industrial process without the use of any high-shear special device. Further provided is a high-purity lactic acid-glycolic acid copolymer which has small amounts of dimers such as residual lactid…
Who is the assignee on this patent?
Mitsui Chemicals Inc
What technology area does this patent fall under?
Primary CPC classification C08G63/90. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Jul 03 2018 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).