Polymer treatment for separating volatile material
View Patent ↗A process for the separation of volatile material from particulate polymer which has been substantially freed from unreacted monomer in an earlier separation step, comprising (a) feeding the particulate polymer to a purge vessel, optionally causing it to move through the vessel in substantially plug-flow mode, (b) heating the particulate polymer in the purge vessel to a temperature greater than 30° C. but insufficiently high to cause the particles to become agglomerated, and/or maintaining the polymer at a temperature in this range in the purge vessel, (c) feeding air to the purge vessel counter-current to the movement of the particulate polymer to remove volatile material therefrom, (d) removing the particulate polymer from the purge vessel. Preferably the particulate polymer fed to the purge vessel is caused to move through the vessel in substantially plug-flow mode. The process is particularly suitable for polyethylene.
1. A process for the separation of volatile material from particulate polymer particles which have been substantially freed from unreacted monomer in an earlier separation step, comprising
(a) feeding the particulate polymer particles to a purge vessel,
(b) heating the particulate polymer particles while they move through the purge vessel to a temperature greater than 30° C. but insufficiently high to cause the particles to become agglomerated, and/or maintaining the particulate polymer particles at a temperature in this range in the purge vessel,
(c) feeding air to the purge vessel counter-current to the movement of the particulate polymer particles to remove volatile material therefrom, and
(d) removing the particulate polymer particles from the purge vessel.
2. A process as claimed in claim 1 wherein the particulate polymer particles are preheated before entering the purge vessel.
3. A process as claimed in claim 1 wherein the polymer is a polyolefin.
4. A process as claimed in claim 3 wherein the polyolefin has been prepared in the gas-phase, the liquid phase, the solution phase or in a high pressure process.
5. A process as claimed in claim 4 wherein the polyolefin is polyethylene.
6. A process as claimed in claim 1 wherein the particulate polymer particles are heated to a temperature no greater than 5° C. below the Vicat softening temperature in the purge vessel and/or are maintained at a temperature in this range in the purge vessel.
7. A process as claimed in claim 1 wherein the quantity of volatile material (excluding water) present in the particulate polymer particles fed to the purge vessel is not greater than 500 ppm by weight.
8. A process as claimed in claim 1 wherein the level of volatiles present in a purge gas stream exiting the purge vessel is not more than about 5 milligrams per litre of gas.
9. A process as claimed in claim 1 wherein the particulate polymer particles are transferred from the purge vessel to a cooling vessel.
10. A process as claimed in claim 1 wherein the particulate polymer particles which are fed to the purge vessel are caused to move through the vessel in substantially plug flow mode.
11. A process as claimed in claim 10 wherein the flow characteristics of the particulate polymer particle in the purge vessel are such that a standard deviation of a residence time is not greater than 50% of a mean residence time of the particulate polymer particles in the purge vessel.
12. A process as claimed in claim 10 wherein the residence time of the particulate polymer particles in the purge vessel lies in the range of from 6 to 10 hours.
13. A process as claimed in claim 10 wherein the particulate polymer particles are moved through the purge vessel using an Archimedean screw device or under the influence of gravity.
14. A process as claimed in claim 13 wherein the particulate polymer particles move under the influence of gravity in response to a continuous removal of solid from a base of the purge vessel.