Continuous process for producing poly (trimethylene terephthalate)
View Patent ↗A continuous process for the production of poly(trimethylene terephthalate) is disclosed. According to the process, a liquid feed mixture comprising bis-3-hydroxypropyl terephthalate and/or low molecular weight polyesters of 1,3-propanediol and terephthalic acid, the liquid feed mixture having a mole ratio of propylene groups to terephthalate groups of 1.1 to 2.2 is fed to a flasher. A first stream of gaseous by-products is continuously vaporized and removed from the flasher, and a liquid flasher reaction product having a mole ratio of propylene groups to terephthalate groups of less than about 1.5 is continuously withdrawn from the flasher. The liquid flasher reaction product is continuously fed to a prepolymerizer where it is continuously polymerized to form a poly(trimethylene terephthalate) prepolymer and a second stream of gaseous by-products. Poly(trimethylene terephthalate) prepolymer having a relative viscosity of at least about 5 is continuously withdrawn from the prepolymerizer and continuously fed to a final polymerizer, where it is continuously polymerized to form a higher molecular weight poly(trimethylene terephthalate) and a third stream of gaseous by-products. Higher molecular weight poly(trimethylene terephthalate) having a relative viscosity of at least about 17 is continuously withdrawn from the final polymerizer.
1. A process comprising:
(a) continuously flashing a liquid feed mixture comprising a catalyst and at least one of bis-3-hydroxypropyl terephthalate and low molecular weight polyesters containing propylene groups from 1,3-propanediol and terephthalate groups to form gaseous by-products and liquid reaction product, wherein gaseous by-products continuously exit the flashing;
(b) continuously withdrawing liquid reaction product from the flashing; and
(c) continuously prepolymerizing the liquid reaction product to form poly(trimethylene terephthalate) prepolymer.
2. The process of claim 1 , wherein the liquid feed mixture is fed to the flashing and has a mole ratio of propylene groups to terephthalate groups of 1.1 to 2.2.
3. The process of claim 1 , wherein the liquid reaction product withdrawn from the flashing has a mole ratio of propylene groups from 1,3-propanediol to terephthalate groups of less than about 1.5.
4. The process of claim 2 , wherein the liquid reaction product withdrawn from the flashing has a mole ratio of propylene groups from 1,3-propanediol to terephthalate groups of less than about 1.5.
5. The process of claim 1 , wherein the prepolymer has a relative viscosity of at least about 5.
6. The process of claim 5 , wherein the prepolymer has a relative viscosity of about 5 to 7.
7. A process comprising:
(a) continuously flashing a liquid feed mixture comprising a catalyst and at least one of bis-3-hydroxypropyl terephthalate and low molecular weight polyesters containing propylene groups from 1,3-propanediol and terephthalate groups, to form gaseous by-products and liquid reaction product, wherein gaseous by-product continuously exits the flashing;
(b) continuously prepolymerizing the liquid reaction product to form poly(trimethylene terephthalate) prepolymer; and
(c) continuously polymerizing the poly(trimethylene terephthalate) prepolymer to form a higher molecular weight poly(trimethylene terephthalate).
8. The process of claim 7 , wherein the liquid feed mixture has a mole ratio of propylene groups from 1,3-propanediol to terephthalate groups of 1.1 to 2.2.
9. The process of claim 7 , wherein the liquid reaction product withdrawn from the flashing has a mole ratio of propylene groups from 1,3-propanediol to terephthalate groups of less than about 1.5.
10. The process of claim 8 , wherein the liquid reaction product withdrawn from the flashing has a mole ratio of propylene groups from 1,3-propanediol to terephthalate groups of less than about 1.5.
11. The process of claim 7 , wherein the higher molecular weight poly(trimethylene terephthalate) has a relative viscosity of at least about 17.
12. The process of claim 8 , wherein the higher molecular weight poly(trimethylene terephthalate) has a relative viscosity of at least about 17.
13. The process of claim 9 , wherein the higher molecular weight poly(trimethylene terephthalate) has a relative viscosity of at least about 17.
14. The process of claim 10 , wherein the higher molecular weight poly(trimethylene terephthalate) has a relative viscosity of at least about 17.
15. The process of claim 14 , wherein the higher molecular weight poly(trimethylene terephthalate) has a relative viscosity of at least about 35.
16. The process of claim 15 , wherein the higher molecular weight poly(trimethylene terephthalate) has a relative viscosity of at least about 40.
17. The process of claim 16 , wherein the higher molecular weight poly(trimethylene terephthalate) has a relative viscosity of at least about 45.
18. The process of claim 17 , wherein the higher molecular weight poly(trimethylene terephthalate) has a relative viscosity of at least about 50.
19. A process comprising:
(a) continuously flashing a liquid feed mixture comprising a catalyst and at least one of bis-3-hydroxypropyl terephthalate and low molecular weight polyesters containing propylene groups from 1,3-propanediol and terephthalate groups, thereby forming first gaseous by-products and liquid reaction product;
(b) continuously removing the gaseous by-products from the flashing;
(c) continuously withdrawing liquid reaction product from the flashing;
(d) continuously prepolymerizing the liquid reaction product to form poly(trimethylene terephthalate) prepolymer and second gaseous by-products;
(e) continuously withdrawing poly(trimethylene terephthalate) prepolymer from the prepolymerizing;
(f) continuously polymerizing the poly(trimethylene terephthalate) prepolymer to form a higher molecular weight poly(trimethylene terephthalate) and third gaseous products; and
(g) continuously withdrawing the higher molecular weight poly(trimethylene terephthalate) from the polymerization.
20. The process of claim 19 , wherein the liquid feed mixture has a mole ratio of propylene groups from 1,3-propanediol to terephthalate groups of 1.1 to 2.2.
21. The process of claim 19 , wherein the liquid reaction product withdrawn from the flashing has a mole ratio of propylene groups from 1,3-propanediol to terephthalate groups of less than about 1.5.
22. The process of claim 20 , wherein the liquid reaction product withdrawn from the flashing has a mole ratio of propylene groups from 1,3-propanediol to terephthalate groups of less than about 1.5.
23. The process of claim 19 , wherein the higher molecular weight poly(trimethylene terephthalate) has a relative viscosity of at least about 17.
24. The process of claim 20 , wherein the higher molecular weight poly(trimethylene terephthalate) has a relative viscosity of at least about 17.
25. The process of claim 21 , wherein the higher molecular weight poly(trimethylene terephthalate) has a relative viscosity of at least about 17.
26. The process of claim 22 , wherein the higher molecular weight poly(trimethylene terephthalate) has a relative viscosity of at least about 17.
27. The process of claim 26 , wherein the higher molecular weight poly(trimethylene terephthalate) has a relative viscosity of at least about 35.
28. The process of claim 27 , wherein the higher molecular weight poly(trimethylene terephthalate) has a relative viscosity of at least about 40.
29. The process of claim 28 , wherein the higher molecular weight poly(trimethylene terephthalate) has a relative viscosity of at least about 45.
30. The process of claim 29 , wherein the higher molecular weight poly(trimethylene terephthalate) has a relative viscosity of at least about 50.
31. The process according to claim 19 , wherein the first gaseous by-products are continuously removed from the flasher and condensed, the second gaseous by-products are continuously removed from the prepolymerizer and condensed, and the combined first and second condensed by-products contain not more than 100 ppm by weight of acrolein and not more than 600 ppm of allyl alcohol.
32. The process according to claim 31 , wherein the combined first and second condensed by-products contain not more than 60 ppm by weight of acrolein and not more than 400 ppm of allyl alcohol.
33. The process according to claim 31 , wherein the combined first and second condensed by-products contain not more than 40 ppm by weight of acrolein and not more than 250 ppm of allyl alcohol.
34. The process according to claim 19 , wherein the third gaseous by-products are continuously removed from the final polymerizer and condensed, and the third condensed by-products contain not more than 200 ppm of acrolein and not more than 3000 ppm of allyl alcohol.
35. The process according to claim 34 , wherein the third condensed by-products contain not more than 100 ppm of acrolein and not more than 2500 ppm of allyl alcohol.
36. The process according to claim 34 , wherein the third condensed by-products contain not more than 70 ppm of acrolein and not more than 1000 ppm of allyl alcohol.
37. A continuous process for the production of poly(trimethylene terephthalate) comprising the steps of:
(a) continuously flashing a liquid feed mixture, the liquid feed mixture comprising a catalyst and at least one of bis-3-hydroxypropyl terephthalate and low molecular weight polyesters containing propylene groups from 1,3-propanediol and terephthalate groups, and the liquid feed mixture having a mole ratio of propylene groups from 1,3-propanediol to terephthalate groups of 1.1 to 2.2;
(b) continuously vaporizing by-products in the flashing and removing the by-products from the flashing in a first stream of gaseous by-products, and continuously withdrawing a liquid flasher reaction product having a mole ratio of propylene groups from 1,3-propanediol to terephthalate groups of less than about 1.5 from the flashing;
(c) continuously prepolymerizing the liquid flasher reaction product to form a poly(trimethylene terephthalate) prepolymer and a second stream of gaseous by-products;
(d) continuously withdrawing the poly(trimethylene terephthalate) prepolymer from the prepolymerizer;
(e) continuously polymerizing the poly(trimethylene terephthalate) prepolymer to form a higher molecular weight poly(trimethylene terephthalate) and a third stream of gaseous by-products; and
(f) continuously withdrawing the higher molecular weight poly(trimethylene terephthalate) from the final polymerizer, the higher molecular weight poly(trimethylene terephthalate) having a relative viscosity of at least about 17.