Poly(3-hydroxybutyrate) resin tube and method for producing same
US-2025066605-A1 · Feb 27, 2025 · US
US2021301127A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2021301127-A1 |
| Application number | US-201917266676-A |
| Country | US |
| Kind code | A1 |
| Filing date | Aug 19, 2019 |
| Priority date | Aug 20, 2018 |
| Publication date | Sep 30, 2021 |
| Grant date | — |
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Provided is a poly(3-hydroxybutyrate) resin tube including a poly(3-hydroxybutyrate) resin, the tube having a wall thickness of 0.1 to 0.6 mm. The difference between the melting point peak temperature and the melting point peak end temperature in differential scanning calorimetry analysis of the poly(3-hydroxybutyrate) resin is preferably 10° C. or higher. Preferably, production of the tube includes the step of melting a poly(3-hydroxybutyrate) resin in an extruder, then extruding the resin from an annular die, and introducing the resin into water, the annular die temperature being set to a temperature between the melting point peak temperature and the melting point peak end temperature in differential scanning calorimetry analysis of the poly(3-hydroxybutyrate) resin.
Opening claim text (preview).
1 . A poly(3-hydroxybutyrate) resin tube, comprising; a poly(3-hydroxybutyrate) resin, wherein the tube has a wall thickness of 0.1 to 0.6 mm. 2 . The poly(3-hydroxybutyrate) resin tube according to claim 1 , wherein a difference between a melting point peak temperature and a melting point peak end temperature in differential scanning calorimetry analysis of the poly(3-hydroxybutyrate) resin is 10° C. or higher. 3 . The poly(3-hydroxybutyrate) resin tube according to claim 1 , wherein the poly(3-hydroxybutyrate) resin is poly (3-hydroxybutyrate-co-3-hydroxyhexanoate). 4 . A method for producing the poly(3-hydroxybutyrate) resin tube of claim 1 , the method comprising: melting a poly(3-hydroxybutyrate) resin in an extruder; extruding the melted poly(3-hydroxybutyrate) resin from an annular die; and introducing the extruded poly(3-hydroxybutyrate) resin into water, wherein a temperature of the annular die is set to be between a melting point peak temperature and a melting point peak end temperature in differential scanning calorimetry analysis of the poly(3-hydroxybutyrate) resin. 5 . The method according to claim 4 , wherein the poly(3-hydroxybutyrate) resin has a melt viscosity at 160° C. of 10,000 poise or more. 6 . The method according to claim 4 , further comprising: mixing at least two types of poly(3-hydroxybutyrate) resins. 7 . The poly(3-hydroxybutyrate) resin tube according to claim 1 , wherein the poly(3-hydroxybutyrate) resin has a melt viscosity at 160° C. of 10,000 poise or more. 8 . The poly(3-hydroxybutyrate) resin tube according to claim 1 , wherein a difference between a melting point peak temperature and a melting point peak end temperature in differential scanning calorimetry analysis of the poly(3-hydroxybutyrate) resin is 12° C. or higher and 50° C. or lower. 9 . The poly(3-hydroxybutyrate) resin tube according to claim 1 , wherein the tube comprises a plurality of tubes having different diameters connectable with a stopper portion such that the tube is extensible. 10 . The poly(3-hydroxybutyrate) resin tube according to claim 1 , wherein the tube has a bellows portion such that the tube is bendable at the bellows portion. 11 . The poly(3-hydroxybutyrate) resin tube according to claim 1 , wherein the poly(3-hydroxybutyrate) resin comprises at least two types of poly(3-hydroxybutyrate) resins. 12 . The poly(3-hydroxybutyrate) resin tube according to claim 1 , wherein the tube has an outer diameter of from 2 to 10 mm and a length of from 50 to 350 mm. 13 . The poly(3-hydroxybutyrate) resin tube according to claim 1 , wherein the poly(3-hydroxybutyrate) resin has a melt viscosity at 160° C. of 13,000 poise or more and 30,000 poise or less.
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