Process for making polyethylene terephthalate
The invention relates to a process for making polyethylene terephthalate (PET) from ethylene glycol (EG), purified terephthalic acid (PTA) and optionally up to 6 mol % comonomer, using a mixed metal catalyst system and comprising the steps of a) esterifying EG and PTA to form diethyleneglycol terephthalate and oligomers (DGT), and b) melt-phase polycondensing DGT to form PET and EG, wherein the catalyst system substantially consists of 70-160 ppm of Sb-compound, 20-70 ppm of Zn-compound, and 0.5-20 ppm of Ti-glycolate as active components (ppm metal based on PET). With this process that applies reduced amount of metal catalyst components PET can be obtained with high productivity, which polyester shows favorable color and optical clarity, also if recycling of EG is applied within the process.
1. Process for making polyethylene terephthalate (PET) from ethylene glycol (EG), purified terephthalic acid (PTA) and optionally up to 6 mol % comonomer, using a mixed metal catalyst system and comprising:
a) esterifying EG and PTA to form diethylene glycol terephthalate and oligomers (DGT), and
b) melt-phase polycondensing DGT to form PET and EG,
wherein the catalyst system substantially consists of a Sb-compound, a Zn-compound and Ti-glycolate as active components, at concentration of 70-160 ppm Sb, 20-70 ppm Zn and 0.5-20 ppm Ti (ppm metal based on PET), and optionally a P-compound.
2. The process according to claim 1 , wherein the comonomer is present in an amount of 0.5-5 mol %, and wherein the comonomers comprise at least one comonomer selected from the group consisting of isophthalic acid, diethylene glycol and 1,4-cyclohexanedimethanol is applied.
3. The process according to claim 1 , further comprising subsequent steps of
c) forming the polyester into pellets,
d) crystallising the pellets, and
e) solid-state polycondensing the polyester.
4. The process according to claim 1 , wherein the PET obtained has IV of at least 0.7 dL/g.
5. The process according to claim 1 , wherein EG removed from polycondensation step b) is recycled back to esterification step a).
6. The process according to claim 1 , wherein the catalyst system substantially consists of 120-145 ppm Sb, 30-45 ppm Zn, and 1.0-4.0 ppm Ti (elemental contents based on PET).
7. The process according to claim 1 , wherein total amount of metal components in the catalyst system is less than 190 ppm.
8. The process according to claim 1 , wherein the catalyst system further comprises 10-50 ppm of a P-compound.
9. Process for making polyethylene terephthalate (PET) comprising:
a) esterifying ethylene glycol (EG) and purified terephthalic acid (PTA) and at least 0.5 mol % comonomer to form diethylene glycol terephthalate and oligomers (DGT) in the presence of a mixed metal catalyst system, and
b) melt-phase polycondensing DGT to form PET and EG,
wherein the catalyst system substantially consists of a Sb-compound, a Zn-compound and Ti-glycolate as active components, at concentration of 70-160 ppm Sb, 20-70 ppm Zn and 0.5-20 ppm Ti (ppm metal based on PET).
10. The process according to claim 9 , wherein the catalyst system substantially consists of 120-145 ppm Sb, 30-45 ppm Zn, and 1.0-4.0 ppm Ti (elemental contents based on PET).
11. The process according to claim 9 , wherein the comonomer comprises a material selected from di-carboxylic acids and their ester-forming derivatives, polycarboxylic acids and their ester-forming derivatives, di-hydroxy compounds and their ester-forming derivatives, poly-hydroxy compounds and their ester-forming derivatives, and hydroxycarboxylic acids and their ester-forming derivatives.
12. The process according to claim 1 , wherein the P-compound is present, and wherein the P-compound is added during transfer of the DGT to a subsequent reaction vessel for performing step b).
13. The process according to claim 1 , wherein the P-compound is present, and wherein the P-compound is added at the beginning of step b).
14. Process for making polyethylene terephthalate (PET) from ethylene glycol (EG), purified terephthalic acid (PTA) and optionally up to 6 mol % comonomer, using a mixed metal catalyst system and comprising:
a) esterifying EG comprising virgin EG and recycled EG and PTA to form diethylene glycol terephthalate and oligomers (DGT), and
b) melt-phase polycondensing DGT to form PET and EG,
wherein the catalyst system substantially consists of a Sb-compound, a Zn-compound and Ti-glycolate as active components, at concentration of 70-160 ppm Sb, 20-70 ppm Zn and 0.5-20 ppm Ti (ppm metal based on PET), and optionally a P-compound; and
wherein the PET formed has an intrinsic viscosity (IV) of at least 0.7 dL/g.
15. The process according to claim 14 , wherein the IV is from 0.75 to 0.85 dL/g.
16. The process according to claim 14 , wherein the P-compound is added during transfer of the DGT to a subsequent reaction vessel for performing step b).
17. The process according to claim 14 , wherein the P-compound is added at the beginning of step b).
18. The process according to claim 14 , wherein the PET is made from the EG, and the comonomer.