초록 ▼

A method and apparatus for underwater pelletizing and subsequent drying of polyethylene terephthalate (PET) polymers and other high temperature crystallizing polymeric materials to crystallize the polymer pellets without subsequent heating. High velocity air or other inert gas is injected into the w

A method and apparatus for underwater pelletizing and subsequent drying of polyethylene terephthalate (PET) polymers and other high temperature crystallizing polymeric materials to crystallize the polymer pellets without subsequent heating. High velocity air or other inert gas is injected into the water and pellet slurry line to the dryer near the pelletizer exit. The slurry line has a substantially straight component, and air is preferably injected at the end of the straight component nearest the pelletizer exit and in a direction substantially coincident with the axis of the straight component. The air injection significantly increases the speed of the pellets into and out of the dryer such that the PET polymer pellets leave the dryer above at least 135° C., and preferably above 145° C., to self-initiate crystallization.

대표청구항 ▼

The invention claimed is: 1. A method for processing crystallizing polymeric materials into pellets, which comprises: extruding into strands a crystallizing polymeric material having sufficient heat for crystallization; cutting the extruded strands into pellets in a water stream; transporting said

The invention claimed is: 1. A method for processing crystallizing polymeric materials into pellets, which comprises: extruding into strands a crystallizing polymeric material having sufficient heat for crystallization; cutting the extruded strands into pellets in a water stream; transporting said pellets in said water stream as a water and pellet slurry; injecting an inert gas at a high velocity into said pellet and water slurry such that said pellets retain sufficient heat for crystallization of said polymeric material; drying said pellets in a dryer; and crystallizing said pellets after exiting said dryer without a second heating stage. 2. The method of claim 1 wherein said material includes polyethylene terephthalate polymer. 3. The method of claim 1 wherein the gas injected into said slurry increases pellet flow speed from a pelletizer at said step of extrusion to dryer exit to a rate of less than about one second. 4. The method of claim 1 wherein said polymeric material is a high temperature crystallizing polymeric material and said pellets are cooled in said water stream. 5. A method for processing polyethylene terephthalate polymers into pellets using an apparatus including an underwater pelletizer and a dryer, said method comprising: extruding strands of polyethylene terephthalate polymer through a die plate for cutting in said underwater pelletizer; cutting the polyethylene terephthalate polymer strands into pellets in a cutting chamber of said pelletizer; transporting said polyethylene terephthalate pellets out of said cutting chamber as a water and pellet slurry; and injecting a high velocity gas into said water and pellet slurry to convert the water into a water vapor mist and enhance the speed of the pellets into and out of said dryer, with said pellets retaining sufficient internal heat upon exiting said dryer for crystallization of said pellets; and crystallizing said pellets after exiting said dryer without a second heating stage. 6. The method as claimed in 5 wherein said polyethylene terephthalate pellets exiting said dryer are placed in a heat insulating container. 7. The method as claimed in claim 5 wherein said polyethylene terephthalate pellets exit said dryer at a mean temperature above about 135° C. 8. The method as claimed in claim 7 wherein said polyethylene terephthalate pellets exit said dryer at a temperature above about 145° C. 9. The method as claimed in claim 5 wherein said step of transporting said polyethylene terephthalate pellets out of said pelletizer to said dryer includes substantially straight transporting said slurry upwardly at an angle from the vertical between 30° and 60°. 10. The method as claimed in claim 9 wherein said angle is about 45°. 11. The method as claimed in claim 5 wherein said pressurized gas is air. 12. The method as claimed in claim 5 wherein said gas is injected substantially in alignment with a flow direction of said water and pellet slurry. 13. The method as claimed in claim 5 wherein said high velocity gas is injected at a flow rate of at least about 100 cubic meters per hour at a pressure of about 8 bar. 14. The method as claimed in claim 5 wherein said vapor mist has' a gas component of about 98% by volume. 15. The method of claim 5 wherein the gas injected into said slurry increases pellet flow speed from the pelletizer to an exit of said dryer to a rate of less than about one second. 16. A method for processing polyethylene terephthalate polymers into crystallized pellets using an apparatus having an underwater pelletizer, a centrifugal dryer and transportation piping therebetween, said method comprising: cutting polyethylene terephthalate polymer strands into pellets in the underwater pelletizer; transporting said pellets out of said pelletizer and into said transportation piping as a water and pellet slurry; introducing a high velocity inert gas into said water and pellet slurry in said transportation piping to separate the water from the pellets; and transporting all of said water and pellets into said centrifugal dryer located downstream of said gas introduction, said pellets exiting said dryer with sufficient internal heat for crystallization of said pellets. 17. The method of claim 16 wherein the gas introduced into said slurry increases a speed of pellet flow from said pelletizer to an exit of said dryer to a rate of less than about one second. 18. The method of claim 16 wherein said step of introducing a high velocity gas includes injecting said gas at a flow rate of about 100 cubic meters per hour at a pressure of about 8 bar. 19. The method of claim 18 wherein said injected gas produces a water vapor mist having a gas component of about 98% by volume. 20. The method of claim 16 wherein crystallization of said pellets occurs using only said internal heat retained from extrusion and in an absence of any secondary heating step while passing through said apparatus.