Polymer stream transfer
View Patent ↗Process for heating a polymer-containing stream being transferred from a polymerization reactor to a separation zone or device, by passing the stream through a heater having at least one transfer line for the stream and a heater for heating the transfer line. The average particle size of the solid polymer is less than 3mm, the mass flowrate of the polymer-containing stream exiting the heater is no more than 15% greater than the mass flowrate exiting the reactor, the average velocity of the polymer-containing stream either at a point 80% along the length of the heated part of the transfer line measured from the transfer line inlet, or at the transfer line outlet, is at least 6 m/s, and the pressure drop across the transfer line per unit length is between 0.0125 bar/m and 0.1 bar/m.
1. Process for heating a polymer-containing stream being transferred from a polymerization reactor to a separation zone or device, comprising passing the stream through a heater comprising at least one transfer line for the stream and a heater for heating the transfer line, wherein the average particle size of the solid polymer is less than 3 mm, the mass flowrate of the polymer-containing stream exiting the heater is no more than 15% greater than the mass flowrate exiting the reactor, the average velocity of the polymer-containing stream either at a point 80% along the length of the heated part of the transfer line measured from the transfer line inlet, or at the transfer line outlet, is at least 6 m/s, and the pressure drop across the transfer line per unit length is between 0.0125 bar/m and 0.1 bar/m.
2. Process according to claim 1 , wherein the average velocity of the polymer-containing stream at 80% along the length of the heated part of the transfer line measured from the transfer line inlet is equal to or greater than its average velocity at 20% along the length of the heated part of the transfer line.
3. Process according to claim 1 , wherein the average particle size of the solid polymer is less than 2 mm.
4. Process according to claim 1 , wherein the mass flowrate of the polymer-containing stream exiting the heater is substantially the same as the mass flowrate exiting the reactor.
5. Process according to claim 1 , wherein the ratio of the average velocity of the polymer-containing stream at 80% along the length of the heated part of the transfer line to its average velocity at 20% along the length of the heated part of the transfer line is greater than 1.1.
6. Process according to claim 1 , wherein the average velocity of the polymer-containing stream at 60% along the length of the heated part of the transfer line measured from the transfer line inlet is equal to or greater than its average velocity at 20% along the length of the heated part of the transfer line.
7. Process according to claim 1 , wherein the ratio of the transfer line's diameter 80% along its heated length, D 80 , to the diameter 20% along its heated length, D 20 , is greater than 1.
8. Process according to claim 1 , wherein the temperature of the internal surface of the transfer line from 50% to 100% along its heated length is maintained below the softening point of the polymer.
9. Process according to claim 1 , wherein the heat input to the polymer-containing stream is adjusted by changing the temperature of the heating medium in contact with the outer surface, and/or by changing the size of the heated area of the transfer line.
10. Process according to claim 1 , wherein the average velocity of the polymer-containing stream either at a point 80% along the length of the heated part of the transfer line measured from the transfer line inlet, or at the transfer line outlet, is at least 8 m/s.
11. Process according to claim 1 , wherein the average velocity of the polymer-containing stream either at a point 80% along the length of the heated part of the transfer line measured from the transfer line inlet, or at the transfer line outlet, is at least 10 m/s.
12. Process according to claim 1 , wherein the pressure drop across the transfer line per unit length is between 0.0125 bar/m and 0.04 bar/m.
13. Process according to claim 3 , wherein the average particle size of the solid polymer is less than 1 mm.
14. Process according to claim 5 , wherein the ratio of the average velocity of the polymer-containing stream at 80% along the length of the heated part of the transfer line to its average velocity at 20% along the length of the heated part of the transfer line is greater than 1.3.
15. Process according to claim 7 , wherein the ratio of the transfer line's diameter 80% along its heated length, D 80 , to the diameter 20% along its heated length, D 20 , is greater than 1.2.
16. Process according to claim 7 , wherein the ratio of the transfer line's diameter 80% along its heated length, D 80 , to the diameter 20% along its heated length, D 20 , is greater than 1.3.
17. Process according to claim 8 , wherein the temperature of the internal surface of the transfer line along all of its heated length is maintained below the softening point of the polymer.