Polyolefin Film and Method for Manufacturing Polyolefin Film
US-2024392083-A1 · Nov 28, 2024 · US
US2016354510A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016354510-A1 |
| Application number | US-201514728177-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jun 2, 2015 |
| Priority date | Jun 2, 2015 |
| Publication date | Dec 8, 2016 |
| Grant date | — |
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Absorbable medical devices based on novel foams and films made from semi-crystalline, segmented copolymers of lactide and epsilon-caprolactone exhibiting long term absorption characteristics are disclosed. Also disclosed are methods of producing said foams and films, and useful polymer solutions.
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We claim: 1 . An absorbable foam, comprising a semicrystalline absorbable segmented copolymer, said copolymer comprising repeating units of polymerized lactide and polymerized epsilon-caprolactone, wherein the mole ratio of polymerized lactide to polymerized epsilon-caprolactone is between about 60:40 to about 75:25, said copolymer having a first heat Tg, as determined by differential scanning calorimetry at a scan rate of 10° C. per minute, equal to or less than 0° C., and a crystallinity level of about 20 percent to about 50 percent, as measured by wide angle X-ray diffraction. 2 . The foam of claim 1 in which the solids content is between about 3 weight percent to about 30 weight percent. 3 . The foam of claim 2 having a solid content between 5 weight percent and 20 weight percent. 4 . The foam of claim 1 having a thickness between about 20 mils to about 500 mils. 5 . The foam of claim 4 having a thickness between about 40 mils and about 200 mils. 6 . The foam of claim 1 having mechanical integrity at least 40 days post-implantation or having mechanical integrity after at least 40 days of incubation in a buffer of pH 7.27 at 37° C. 7 . The foam of claim 1 having mechanical integrity at least 64 days post-implantation or having mechanical integrity after at least 64 days of incubation in a buffer of pH 7.27 at 37° C. 8 . The foam of claim 1 having a crystallinity level great than about 25 percent. 9 . The foam of claim 1 , wherein the copolymer has an inherent viscosity at least about 0.5 dL/g, as measured in a 0.1 g/dl solution of HFIP at 25° C. 10 . A method of making an absorbable foam by a melt process, comprising the steps of: A. providing an absorbable polymer comprising a semicrystalline absorbable segmented copolymer, said copolymer comprising repeating units of polymerized lactide and polymerized epsilon-caprolactone, wherein the mole ratio of polymerized lactide to polymerized epsilon-caprolactone is between about 60:40 to about 75:25, said copolymer having a first heat Tg, as determined by differential scanning calorimetry at a scan rate of 10° C. per minute, equal to or less than 0° C., and a crystallinity level of about 20 to about 50 percent, as measured by wide angle X-ray diffraction, said copolymer having a melt temperature; B. heating the copolymer above the melt temperature to form a melt; C. introducing a suitable blowing agent (chemical or physical) into the melt; and D. enabling the gas produced from the blowing agent to expand within the melt to form an absorbable foam. 11 . A method of making an absorbable foam by a melt process, comprising the steps of: A. providing an absorbable polymer comprising a semicrystalline absorbable segmented copolymer, said copolymer comprising repeating units of polymerized lactide and polymerized epsilon-caprolactone, wherein the mole ratio of polymerized lactide to polymerized epsilon-caprolactone is between about 60:40 to about 75:25, said copolymer having a first heat Tg, as determined by differential scanning calorimetry at a scan rate of 10° C. per minute, equal to or less than 0° C., and a crystallinity level of about 20 to about 50 percent, as measured by wide angle X-ray diffraction, said copolymer having a melt temperature; B. transferring the said absorbable polymer to the hopper of a melt extruder outfitted with a profile die, with a barrel outfitted with a gas injection port, and die heated to a temperature within the range of about 10° C. above the melt temperature of said absorbable polymer to about 270° C. to form a melt; C. extruding said absorbable polymer through said profile die, while injecting into the melt through the gas injection port a gas selected from the group of carbon dioxide, nitrogen, helium, and argon, resulting in a foam; and, D. collecting said foam at a rate to result in a foam thickness between about 0.1 mils and 50 mils. 12 . A method of making an absorbable foam by a melt process, comprising the steps of: A. providing an absorbable polymer comprising a semicrystalline absorbable segmented copolymer, said copolymer comprising repeating units of polymerized lactide and polymerized epsilon-caprolactone, wherein the mole ratio of polymerized lactide to polymerized epsilon-caprolactone is between about 60:40 to about 75:25, said copolymer having a first heat Tg, as determined by differential scanning calorimetry at a scan rate of 10° C. per minute, equal to or less than 0° C., and a crystallinity level of about 20 to about 50 percent, as measured by wide angle X-ray diffraction, said copolymer having a melt temperature; B. transferring the said absorbable polymer in combination with a solid blowing agent to the hopper of a melt extruder outfitted with a profile die, and die heated to a temperature within the range of about 10° C. above the melt temperature of said absorbable polymer to about 270° C.; C. extruding said absorbable polymer through said profile die, resulting in a foam; and, D. collecting said foam at a rate to result in a foam thickness between about 0.1 mils and 50 mils. 13 . A method of making an absorbable foam by a lyophilization process, comprising the steps of: A. providing an absorbable polymer comprising a semicrystalline absorbable segmented copolymer, said copolymer comprising repeating units of polymerized lactide and polymerized epsilon-caprolactone, wherein the mole ratio of polymerized lactide to polymerized epsilon-caprolactone is between about 60:40 to about 75:25, said copolymer having a first heat Tg, as determined by differential scanning calorimetry at a scan rate of 10° C. per minute, equal to or less than 0° C., and a crystallinity level of about 20 to about 50 percent, as measured by wide angle X-ray diffraction; B. dissolving a sufficient quantity of the copolymer in a suitable solvent to form a lyophilizing solution; C. pouring at least a part of the solution into a suitable mold; and, D. subjecting the solution in the mold to a lyophilizing process to form an absorbable foam. 14 . The method of claim 13 wherein the solvent is selected from the group consisting of 1,4-dioxane, trioxane, a mixture of at least 90 weight percent 1,4-dioxane and no more than 10 weight percent water, and a mixture of at least 90 weight percent 1,4-dioxane and no more than 10 weight percent of an organic alcohol having a molecular weight of less than 1500 Daltons. 15 . The method of claim 13 wherein the dissolved absorbable polymer is between about 3 to about 30 percent by weight of the solution. 16 . The method of claim 13 wherein the resulting foam has a thickness between about 20 to about 500 mils. 17 . A lyophilizing solution, comprising: A. a solvent selected from the group consisting of 1,4-dioxane, trioxane, a mixture of at least 90 weight percent 1,4-dioxane and no more than 10 weight percent water, and a mixture of at least 90 weight percent 1,4-dioxane and no more than 10 weight percent of an organic alcohol having a molecular weight of less than 1500 Daltons; and, B. about 3 wt. % to about 30 wt. % of a polymer comprising a semicrystalline absorbable segmented copolymer, the copolymer comprising repeating units of polymerized lactide and polymerized epsilon-caprolactone, wherein the mole ratio of polymerized lactide to polymerized epsilon-caprolactone is between about 60:40 to about 75:25, said copolymer having a first heat Tg, as determined by differential scanning calorimetry at a scan rate of 10° C. per minute, equal to or less than 0° C., and a crystallinity level of about 20 to about 50 percent, as measured
Polyesters derived from hydroxycarboxylic acids, e.g. lactones (C08L67/06 takes precedence) · CPC title
Manufacture of cellular products · CPC title
Materials at least partially resorbable by the body · CPC title
obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds {(A61L31/041 takes precedence)} · CPC title
by elimination of a solid phase from a macromolecular composition or article, e.g. leaching out · CPC title
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