Articles comprising copolyesters produced with germanium catalyst
US-2024376258-A1 · Nov 14, 2024 · US
US10113062B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10113062-B2 |
| Application number | US-201615378919-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 14, 2016 |
| Priority date | Feb 18, 2011 |
| Publication date | Oct 30, 2018 |
| Grant date | Oct 30, 2018 |
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Polymeric compositions and processes of forming the same are discussed herein. The processes generally include contacting a polylactic acid with a reactive modifier selected from epoxy-functionalized polybutadiene, ionic monomer, and combinations thereof.
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What is claimed is: 1. A process for forming a polymeric composition comprising: contacting a polylactic acid with a reactive modifier selected from epoxy-functionalized polybutadiene, ionic monomer, and combinations thereof; and contacting the polylactic acid and the reactive modifier with a polyolefin to produce a polyolefin-polylactic acid blend, wherein the polyolefin exhibits a melt flow rate of less than about 6 dg/min. 2. The process of claim 1 , wherein the polyolefin exhibits a melt flow rate ranging from about 0.5 dg/min. to about 6 dg/min. 3. The process of claim 1 , wherein the polylactic acid is selected from poly(D-lactide), poly(L-lactide), poly(DL-lactide), and combinations thereof. 4. The process of claim 1 , wherein the polylactic acid has a concentration of from about 2 wt. % to about 98 wt. % based on the total weight of the polymeric composition. 5. The process of claim 1 , wherein the reactive modifier contacts the polylactic acid in a concentration of from about 2 wt. % to about 30 wt. % based on the total weight of the polymeric composition. 6. The process of claim 1 , wherein the reactive modifier is an epoxy-functionalized polybutadiene oligomer. 7. The process of claim 6 , wherein the epoxy-functionalized polybutadiene oligomer has a number average molecular weight in a range from about 500 g/mol to about 20000 g/mol. 8. The process of claim 1 , wherein the reactive modifier is an ionic monomer. 9. The process of claim 8 , wherein the ionic monomer is an organometallic salt having acrylate functional groups. 10. The process of claim 1 , wherein the polyolefin is selected from polypropylene, polyethylene, copolymers thereof and combinations thereof. 11. The process of claim 1 , wherein the polyolefin has a concentration of from about 2 wt. % to about 98 wt. % based on the total weight of the polymeric composition. 12. The process of claim 1 , further comprising processing the polymeric composition using fiber extrusion or coextrusion. 13. A process comprising: forming a polymeric composition by contacting a polylactic acid with a reactive modifier selected from epoxy-functionalized polybutadiene, ionic monomer, and combinations thereof; processing the polymeric composition using one or more polymer processing techniques selected from: film, sheet, pipe extrusion or coextrusion, blow molding, injection molding, rotary molding, and thermoforming.
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