US2007187860A1PendingUtilityA1
Direct coupling of melt polymerization and solid state processing for pet
Individually held — no corporate assignee on recordPriority: Sep 16, 2003Filed: Mar 28, 2007Published: Aug 16, 2007
Est. expirySep 16, 2023(expired)· nominal 20-yr term from priority
Inventors:Richard Gill Bonner
B29B 9/06B29K 2067/00B29B 9/16B29B 2009/165B29B 9/00C08G 63/183C08F 2/01
55
PatentIndex Score
0
Cited by
0
References
0
Claims
Abstract
Strands of molten polyethylene terephthalate (PET) from a PET polycondensation reactor are solidified, pelletized, and cooled only to a temperature in the range of 50° C. to a temperature near the polymer Tg by contact with water. The still hot pellets are conveyed, optionally followed by drying to remove water, to a PET crystallizer. By avoiding cooling the amorphous pellets to room temperature with water and cool air, significant savings of energy are realized.
Claims
exact text as granted — not AI-modified1 . A process comprising:
a) pelletizing a molten polyethylene terephthalate to form amorphous polyethylene terephthalate pellets; b) transporting the pellets in a stream of water to a dryer to form a stream of dry or moist pellets, wherein the stream of water has a temperature of 50° C. or more; and c) a crystallization step wherein the stream of dry or moist pellets are crystallized and the stream of dry or moist pellets is introduced into the step of crystallizing at a pellet temperature of 50° C. or more.
2 . The process of claim 1 , wherein the stream of dry or moist pellets are continuously fed from the dryer to the crystallization step.
3 . The process of claim 2 , wherein the dryer is a centrifugal dryer.
4 . The process of claim 3 , wherein said water is separated from the pellets and re-circulated to transport the pellets in said stream of water.
5 . The process of claim 2 , wherein the stream of dry or moist pellets are continuously fed from the dryer to the crystallization step.
6 . The process of claim 1 , wherein the stream of dry or moist pellets are dry.
7 . The process of claim 1 , wherein no external heat is required to maintain the water temperature.
8 . The process of claim 1 , wherein a portion of the water is separated from the water stream through a dewatering screen.
9 . The process of claim 1 , wherein the water in the water stream is at a temperature insufficient to cool the temperature of the pellets in the water stream to below the T g of the pellets.
10 . The process of claim 1 , wherein water present on the surface of the pellets, if any, after the dryer is evaporated prior to the crystallization step.
11 . The process of claim 1 , wherein following the crystallization step, the pellets are solid state polymerized.
12 . The process of claim 1 , wherein the polyethylene terephthalate is a polymer modified with up to 10 mol percent dicarboxylic acids other than terephthalic acid and up to 10 mol percent of diols other than ethylene glycol.
13 . The process of claim 12 , wherein the diols other than ethylene glycol comprise CHDM.
14 . The process of claim 12 , wherein the dicaroxylic acids other than terephthalic acid comprise isophthalic acid.Join the waitlist — get patent alerts
Track US2007187860A1 — get alerts on status changes and closely related new filings.
We store only your email — no account needed. See our privacy policy.