Dissolution of oxidized cellulose
US-10982012-B2 · Apr 20, 2021 · US
US11873350B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11873350-B2 |
| Application number | US-202117233694-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 19, 2021 |
| Priority date | Jun 29, 2011 |
| Publication date | Jan 16, 2024 |
| Grant date | Jan 16, 2024 |
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A process for dissolving modified cellulose is disclosed. The process includes contacting modified cellulose with a solvent in a mixture to form swelled modified cellulose and then contacting the mixture with a salt to dissolve the swelled modified cellulose.
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What is claimed is: 1. A process comprising: forming a mixture by contacting an oxidized cellulose with a solvent to form a swelled oxidized cellulose; adjusting the mixture to a first temperature; contacting the swelled oxidized cellulose with a salt to form an oxidized cellulose solution; and adjusting the oxidized cellulose solution to a second temperature lower than the first temperature, wherein dissolved oxidized cellulose of the oxidized cellulose solution retains from about 80% to about 120% of a degree of oxidation of the oxidized cellulose prior to dissolution or from about 80% to about 120% of a molecular weight of the oxidized cellulose prior to dissolution. 2. The process according to claim 1 , wherein the first temperature is adjusted to a temperature of from about 115° C. to about 145° C. 3. The process according to claim 1 , wherein the first temperature is adjusted to a temperature of from about 120° C. to about 140° C. 4. The process according to claim 1 , wherein the first temperature is adjusted to a temperature of from about 130° C. to about 135° C. 5. The process according to claim 1 , wherein the second temperature is adjusted to a temperature of from about 90° C. to about 120° C. 6. The process according to claim 1 , wherein the second temperature is adjusted to a temperature of from about 100° C. to about 110° C. 7. The process according to claim 1 , wherein the solvent is selected from the group consisting of N,N-Dimethylacetamide, N-methyl-2-pyrrolidinone, and combinations thereof. 8. The process according to claim 1 , wherein the salt is selected from the group consisting of lithium halides, sodium halides, potassium halides, and combinations thereof. 9. The process according to claim 1 , wherein the mixture and the oxidized cellulose solution are formed under an inert atmosphere. 10. A process comprising: forming a mixture by contacting an oxidized cellulose with a solvent to form a swelled oxidized cellulose; adjusting the mixture to a first temperature; contacting the swelled oxidized cellulose with a salt to form an oxidized cellulose solution; adjusting the oxidized cellulose solution to a second temperature lower than the first temperature; and forming a plurality of microspheres from the oxidized cellulose solution. 11. The process according to claim 10 , further comprising: forming an emulsion from the oxidized cellulose solution. 12. The process according to claim 11 , further comprising: contacting the oxidized cellulose solution with at least one bioactive agent to form a discontinuous phase liquid; contacting the discontinuous phase liquid with a continuous phase liquid to form the emulsion; and contacting the emulsion with a third phase liquid to extract the solvent from the emulsion, thereby forming a plurality of modified cellulose microspheres. 13. The process according to claim 12 , wherein the continuous phase liquid is selected from the group consisting of plant-based oils, petroleum-based oils, silicone-based oils, and combinations thereof. 14. The process according to claim 12 , wherein the third phase liquid is miscible with the continuous phase liquid and the discontinuous phase liquid. 15. The process according to claim 14 , wherein the third phase liquid is selected from the group consisting of isopropyl myristate, hexane, triglycerides and combinations thereof. 16. The process according to claim 14 , wherein the third phase liquid is present in an amount from about 130% by volume to about 170% by volume of the continuous phase liquid. 17. The process according to claim 10 , wherein the mixture and the oxidized cellulose solution are formed under an inert atmosphere. 18. A microsphere comprising: solubilized oxidized cellulose having from about 80% to about 120% of a degree of oxidation of undissolved oxidized cellulose prior to dissolution or from about 80% to about 120% of a molecular weight of the undissolved oxidized cellulose prior to dissolution; and at least one bioactive agent. 19. The microsphere according to claim 18 , wherein the bioactive agent is selected from the group consisting of a hydrophilic bioactive agent, a protein therapeutic, a biologic, and combinations thereof. 20. The microsphere according to claim 18 , wherein the microsphere is formed by: contacting an oxidized cellulose solution comprising a solvent with the at least one bioactive agent to form a discontinuous phase liquid; contacting the discontinuous phase liquid with a continuous phase liquid to form an emulsion; and contacting the emulsion with a third phase liquid to extract the solvent from the emulsion. 21. The microsphere according to claim 20 , wherein the third phase liquid is miscible with the continuous phase liquid and the discontinuous phase liquid. 22. The microsphere according to claim 20 , wherein the third phase liquid is selected from the group consisting of isopropyl myristate, hexane, triglycerides and combinations thereof.
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