Articles comprising copolyesters produced with germanium catalyst
US-2024376258-A1 · Nov 14, 2024 · US
US2018142069A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2018142069-A1 |
| Application number | US-201815874632-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jan 18, 2018 |
| Priority date | Aug 29, 2013 |
| Publication date | May 24, 2018 |
| Grant date | — |
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Disclosed herein is a foamable resin composition for a foam sheet including polylactic acid resin particles, each of the particles having a particle size of about 1 μm to about 100 μm. A process for preparing a particulate polylactic acid resin includes: introducing a polylactic acid resin and then forming a molten polylactic acid spray solution; and injecting the molten polylactic acid spray solution by a melt spray method and simultaneously cooling the molten polylactic acid spray solution to obtain a particulate polylactic acid. In addition, disclosed herein is a process for preparing a foam sheet using the foamable resin composition for a foam sheet including a polylactic acid resin.
Opening claim text (preview).
1 . A process for preparing a particulate polylactic acid resin comprising: introducing a polylactic acid resin and then forming a molten polylactic acid spray solution; and spraying the molten polylactic acid spray solution by a melt spray method and simultaneously cooling the molten polylactic acid spray solution to obtain a particulate polylactic acid. 2 . The process according to claim 1 , wherein the polylactic acid resin is introduced into an extruder, and then transferred to an spray nozzle and heated in the spray nozzle to form the molten polylactic acid spray solution. 3 . The process according to claim 2 , wherein the polylactic acid resin in the form of pellet or powder is introduced into the extruder. 4 . The process according to claim 3 , wherein the molten polylactic acid spray solution is introduced into the spray nozzle together with an air and then discharged. 5 . The process according to claim 4 , wherein a temperature of the air that is injected into the spray nozzle is of 300° C. to 500° C., a pressure of the air that is injected into the spray nozzle is of 100 psi to 1,000 psi, and an injection speed of the air that is injected into the spray nozzle is of 10 m/s to 50 m/s. 6 . The process according to claim 2 , wherein a temperature of the spray nozzle is of 200° C. to 400° C. 7 . The process according to claim 2 , wherein a pressure of the spray nozzle is of 10 psi to 1,000 psi. 8 . The process according to claim 2 , wherein a diameter of the spray nozzle is of 0.5 mm to 3.0 mm. 9 . The process according to claim 1 , wherein the molten polylactic acid spray solution comprises at least one additive selected from the group consisting of a lubricant, a plasticizer, and a combination thereof. 10 . The process according to claim 1 , wherein the molten polylactic acid spray solution has a viscosity of 1,500 cps to 2,000 cps at 250° C. 11 . The process according to claim 2 , wherein a voltage of 2,000 V to 50,000 V is applied to the spray nozzle to carry out a melt electrostatic spray deposition. 12 . The process according to claim 1 , wherein the particulate polylactic acid resin has an average particle size of 1 μm to 100 μm.
Biodegradable polymers · CPC title
Expanding without a foaming agent · CPC title
Pulverisation by spraying · CPC title
Particles, powder or granules (expandable particles B29K2105/046) · CPC title
extruding the compound through a flat die (in general B29C48/03) · CPC title
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