A barrier system
US-2024051735-A1 · Feb 15, 2024 · US
US9663589B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9663589-B2 |
| Application number | US-201414767841-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 13, 2014 |
| Priority date | Feb 14, 2013 |
| Publication date | May 30, 2017 |
| Grant date | May 30, 2017 |
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Disclosed herein are processes for providing a biopolymer from a biomass or source of chitin using ionic liquids. The processes involve contacting a biomass or source of chitin with an ionic liquid to produce a biopolymer comprising solution and precipitating the biopolymer from the solution with supercritical CO 2 , gaseous CO 2 , or combinations thereof.
Opening claim text (preview).
What is claimed is: 1. A process for providing a biopolymer from a biomass, comprising: a) contacting an ionic liquid with the biomass to form a biopolymer containing solution, wherein the biomass is a chitinous biomass, the biopolymer comprises chitin, the ionic liquid comprises a cation and an anion, wherein the cation is an imidazolium, and the anion is C 1 -C 6 carboxylate; b) adding supercritical CO 2 to the solution to precipitate the biopolymer from the biopolymer containing solution; and c) removing the CO 2 from the ionic liquid to provide a recycled ionic liquid. 2. The process of claim 1 , further comprising isolating the precipitated biopolymer. 3. The process of claim 1 , wherein the chitinous biomass comprises the shells of crustaceans. 4. The process of claim 1 , wherein the chitinous biomass is selected from the group consisting of shrimp shells, crab shells, lobster shells, crawfish shells, prawn shells, and combinations thereof. 5. The process of claim 1 , wherein the biomass is contacted with the ionic liquid at a temperature of from about 70° C. to about 130° C. 6. The process of claim 1 , wherein the biomass is dissolved or dispersed in the ionic liquid at a temperature of from about 0° C. to about 70° C. 7. The process of claim 1 , wherein in step (a) a microwave is used to heat the biopolymer containing solution. 8. The process of claim 1 , wherein a co-solvent is added to the ionic liquid. 9. The process of claim 1 , wherein an insoluble impurity is present in the biopolymer containing solution and is removed before step (b). 10. The process of claim 9 , wherein the impurity is removed by centrifugation or filtration. 11. The process of claim 1 , wherein the cation is: where each R 1 and R 2 is, independently, a substituted or unsubstituted linear, branched, or cyclic C 1 -C 6 alkyl, or substituted or unsubstituted linear, branched, or cyclic C 1 -C 6 alkoxy; each R 3 , R 4 , and R 5 is, independently, hydrogen, substituted or unsubstituted linear, branched, or cyclic C 1 -C 6 alkyl, substituted or unsubstituted linear, branched, or cyclic C 1 -C 6 alkoxy, or substituted or unsubstituted linear or branched, C 1 -C 6 alkoxyalkyl. 12. The process of claim 1 , wherein the ionic liquid is a 3-alkyl-1-alkyl imidazolium C 1 -C 6 carboxylate. 13. The process of claim 1 , wherein the ionic liquid is 3-ethyl-1-methylimidazolium acetate. 14. The process of claim 1 , wherein step (b) is at a temperature above about 31° C. and a pressure above about 1073 psi (7400 kPa). 15. The process of claim 1 , wherein the recycled ionic liquid is used to contact the biomass. 16. The process of claim 1 , wherein removing the CO 2 from the ionic liquid comprises reducing the pressure and vaporizing the CO 2 from the ionic liquid. 17. A process of using a biopolymer, comprising: a) contacting an ionic liquid with a biomass to form a biopolymer containing solution, wherein the biomass is a chitinous biomass and the biopolymer comprises chitin, wherein the ionic liquid comprises a cation and an anion, wherein the cation is an imidazolium, and wherein the anion is C 1 -C 6 carboxylate; b) adding supercritical CO 2 to the solution to precipitate the biopolymer from the biopolymer containing solution; c) casting the precipitated biopolymer into a fiber, film or bead; and d) removing the CO 2 from the ionic liquid to provide a recycled ionic liquid. 18. The process of claim 17 , further comprising adding an additional polymer or adjunct to the biopolymer containing solution before step (b). 19. The process of claim 18 , wherein the additional polymer is poly(2-hydroxyethyl methacrylate) (poly-HEMA) and the adjunct is a pharmaceutical, herbicide, insecticide, or food ingredient. 20. The process of claim 18 , wherein the additional polymer is poly(lactic acid) (PLA) and the adjunct is a pharmaceutical, herbicide, insecticide, or food ingredient. 21. The process of claim 18 , wherein the additional polymer is polyethylterephthalate, polystyrene, polyethylene, or nylon.
General processes for their isolation or fractionation, e.g. purification or extraction from biomass · CPC title
Lignocellulosic material, e.g. wood, straw or bagasse {(manufacture of articles made from lignocellulosic material by dry processes B27N)} · CPC title
by precipitation from solutions {(C08J3/122 takes precedence)} · CPC title
Cross-Sectional Technologies · mapped topic
Fractionation of cellulose, e.g. separation of cellulose crystallites · CPC title
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