High intrinsic viscosity melt phase polyester polymers with acceptable acetaldehyde generation rates
View Patent ↗A method for the production of solid polyester polymer particles comprising: a) polycondensing a molten polyester polymer composition in the presence of a polycondensation catalyst composition comprising antimony species; b) continuing the polycondenzation of the molten polyester polymer composition to an It.V. of 0.68 dL/g or more; and c) after reaching an It.V. of 0.68 dL/g or more, adding a catalyst stabilizer or deactivator to the polymer melt; and d) after reaching an It.V. of 0.68 dL/g or more, solidifying the melt into solid polyester polymer particles which do not contain organic acetaldehyde scavengers. In a further embodiment, after solidification of the polyester from the melt phase polycondenzation process: e) the amount of residual acetaldehyde in the particles in the solid state is reduced to a level of 10 ppm or less without increasing the It.V. of the particles by more than 0.03 dL/g. Such particles having an AA (acetaldehyde) generation rate of 20 ppm or less upon being melted after solidification following the melt phase production and a free AA level reduced after melt phase production to 10 ppm or less are introduced into a melt processing zone to make articles such as bottle preforms having acceptable levels of residual AA.
1. Finished polyester polymer particles obtained by a process comprising polycondensing a molten polyester polymer composition to an It.V. of at least 0.68dL/g; then adding at least one antimony catalyst stabilizer or deactivator comprising an acidic phosphorous compound to the polymer melt; and then solidifying the polymer melt into solid polyester polymer particles, and having:
a degree of crystallinity of at least 20%,
antimony atoms,
phosphorus atoms,
an acetaldehyde generation rate of less than 20 ppm, as measured at 295° C. for 5 minutes,
lacking organic acetaldehyde scavengers, and
which have not been solid state polymerized,
wherein the molar ratio of phosphorus atoms to antimony atoms, P:Sb, is at least 1:1.
2. The finished particles of claim 1 , wherein the particles have a residual acetaldehyde level of 10 ppm or less.
3. The finished particles of claim 1 , wherein said finished particles comprise a bulk of particles.
4. The finished particles of claim 3 , wherein the bulk is contained in a shipping container.
5. The finished particles of claim 4 , wherein the bulk occupies a volume of at least 10 cubic meters.
6. The finished particles of claim 4 , wherein the particles have an It.V. of at least 0.72 dL/g obtained in the melt phase and a degree of crystallinity of at least 30%.
7. The finished particles of claim 1 , wherein the particles have a b* of 3 or less and an L* of 70 or more.
8. The finished particles of claim 1 , wherein the L* is 76 or more.
9. The finished particles of claim 1 , wherein the antimony atom content ranges from 150 ppm to 300 ppm.
10. The finished particles of claim 1 , wherein the particles are devoid of active titanium species.
11. The finished particles of claim 1 , wherein the It.V. of the particles made in a melt phase production is at least 0.70 dL/g.
12. The finished particles of claim 1 , wherein the phosphorus atoms are obtained from an acidic phosphorus compound.
13. The finished particles of claim 12 , wherein the phosphorus atoms are obtained from phosphoric acid.
14. The finished particles of claim 1 , wherein the level of residual acetaldehyde is 7 ppm or less.
15. The finished particles of claim 1 , wherein the molar ratio of phosphorus atoms to antimony atoms, P:Sb, is 1:1 to 2.1:1 and the phosphorus is present in the form of H 3 PO 4 .
16. The finished particles of claim 1 , wherein the molar ratio of phosphorus atoms to antimony atoms, P:Sb, is 1.5:1 to 2.1:1 and the phosphorus is in the form of H 3 PO 4 .
17. The finished particles of claim 1 , wherein the molar ratio of phosphorus atoms to antimony atoms, P:Sb, is from 1.4:1 to 4.7:1 and the phosphorus is present in the form of H 3 PO 4 .
18. The finished particles of claim 1 , having an It.V that is within +/−0.05 dL/g of the molten polyester polymer composition.