Articles comprising copolyesters produced with germanium catalyst
US-2024376258-A1 · Nov 14, 2024 · US
US2020131308A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2020131308-A1 |
| Application number | US-201916394296-A |
| Country | US |
| Kind code | A1 |
| Filing date | Apr 25, 2019 |
| Priority date | Oct 25, 2018 |
| Publication date | Apr 30, 2020 |
| Grant date | — |
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esterifying the mixture to form a first polyester mixture; and polymerizing the first polyester mixture to form a second polyester mixture, in which the second polyester mixture has a diethylene glycol concentration of less than 1 wt % but greater than 0.1 wt %, based on the total weight of the second polyester mixture, and a polydispersity index of polyethylene terephthalate in the second polyester mixture is less than 3 but greater than 2.
Opening claim text (preview).
What is claimed is: 1 . A manufacturing method of polyester, comprising: mixing Bis(2-Hydroxyethyl) terephthalate monomer with terephthalic acid to form a mixture, wherein the diethylene terephthalate monomer is represented by formula (I) below: esterifying the mixture to form a first polyester mixture; and polymerizing the first polyester mixture to form a second polyester mixture, wherein the second polyester mixture has a diethylene glycol concentration of greater than 0.1 wt % but less than 1 wt %, based on the total weight of the second polyester mixture, and a polydispersity index of polyethylene terephthalate in the second polyester mixture is greater than 2 but less than 3. 2 . The manufacturing method of claim 1 , wherein the mixing the Bis(2-Hydroxyethyl) terephthalate monomer with the terephthalic acid to form the mixture comprises mixing an alkaline substance with the Bis(2-Hydroxyethyl)terephthalate monomer and the terephthalic acid. 3 . The manufacturing method of claim 2 , wherein the alkaline substance comprises tetraethylammonium hydroxide. 4 . The manufacturing method of claim 1 , wherein the second polyester mixture has an intrinsic viscosity in a range from 0.5 to 0.8. 5 . The manufacturing method of claim 1 , wherein the polymerizing the first polyester mixture to form the second polyester mixture comprises adding a catalyst into the first polyester mixture. 6 . The manufacturing method of claim 1 , wherein a molar ratio of the Bis(2-Hydroxyethyl) terephthalate monomer to the terephthalic acid ranges from 1.31:1 to 1.09:1. 7 . The manufacturing method of claim 1 , wherein the first polyester mixture comprises Bis(2-Hydroxyethyl) terephthalate oligomer. 8 . The manufacturing method of claim 7 , wherein the first polyester mixture further comprises diethylene glycol. 9 . The manufacturing method of claim 1 , wherein the manufacturing method is devoid of a step of adding nucleating agents. 10 . A polyester mixture, comprising: polyethylene terephthalate having a polydispersity index of greater than 2 but less than 3; and diethylene glycol, wherein the diethylene glycol has a weight percentage of greater than 0.1 wt % but less than 1 wt %, based on a total weight of the polyester mixture. 11 . The polyester mixture of claim 10 , wherein the polyester mixture has an intrinsic viscosity in a range from 0.5 to 0.8.
Terephthalic acids · CPC title
Antimony or compounds thereof · CPC title
Germanium, antimony, or compounds thereof · CPC title
Preparation processes · CPC title
Non-metals or inter-compounds thereof (boron C08G63/84) · CPC title
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