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The present embodiments provide a system and method for separation within a polymer production process. Specifically, a flashline heater configured according to present embodiments may provide more time than is required for complete vaporization of liquid hydrocarbons that are not entrained within a

The present embodiments provide a system and method for separation within a polymer production process. Specifically, a flashline heater configured according to present embodiments may provide more time than is required for complete vaporization of liquid hydrocarbons that are not entrained within a polymer fluff produced within a polymerization reactor. Such extra time may allow for liquid hydrocarbons that are entrained within the polymer fluff to be vaporized.

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1. A method of separation within a polymer production process, comprising the acts of: receiving a discharged stream in a flashline heater, the discharged stream comprising a liquid part and a solid part upon entry into the flashline heater;heating the discharged stream in the flashline heater as th

1. A method of separation within a polymer production process, comprising the acts of: receiving a discharged stream in a flashline heater, the discharged stream comprising a liquid part and a solid part upon entry into the flashline heater;heating the discharged stream in the flashline heater as the discharged stream passes along a length of the flashline heater such that at least a portion of the liquid part vaporizes to generate a vapor part, wherein a transit time of the discharged stream through the flashline heater is at least approximately 8 seconds; andequilibrating the temperature between the solid part and the vapor part during the at least approximately 8 seconds within the flashline heater. 2. The method of claim 1, wherein equilibrating the temperature comprises heating and reducing the pressure of the discharged stream such that a temperature difference of less than about 1° F. exists between the solid part and the vapor part, and the solid part and the liquid part have respective temperatures within approximately 5° F. of a volatilization temperature of the liquid. 3. The method of claim 1, wherein heating the discharged stream in the flashline heater comprises heating the discharged stream in a first section of the flashline heater and reducing or maintaining the temperature of the discharged stream in a second section of the flashline heater. 4. The method of claim 1, wherein the liquid part comprises a first portion and a second portion, wherein the first portion is not entrained in the solid part and the second portion is entrained in the solid part, and wherein heating the discharged stream within the flashline heater comprises vaporizing substantially all of the first portion at least approximately 2.5 seconds before reaching an exit of the flashline heater. 5. The method of claim 1, comprising receiving the discharged stream in a separation vessel from the flashline heater, vaporizing an additional portion of the liquid part in the separation vessel, discharging at least a portion of the solid part from the separation vessel into a conduit, and providing additional heat to the portion of the solid part within the conduit. 6. A method of separation within a polymer production process, comprising the acts of: receiving a discharged stream in a flashline heater, the discharged stream comprising a liquid diluent and polymer fluff upon entry into the flashline heater, wherein the liquid diluent comprises a first part not entrained in the polymer fluff and a second part entrained within the polymer fluff;heating the discharged stream in the flashline heater as the discharged stream passes along a length of the flashline heater such that at least a portion of the liquid diluent vaporizes to generate vaporized diluent; andequilibrating respective temperatures of the vaporized diluent, the second part of the liquid diluent, and the polymer fluff before the discharged stream exits the flashline heater. 7. The method of claim 6, comprising vaporizing substantially all of the first part of the liquid diluent at least approximately 2.5 seconds before exiting the flashline heater. 8. The method of claim 6, wherein heating the discharged stream in the flashline heater comprises heating the discharged stream such that substantially all of the first part of the liquid diluent and at least a portion of the second part of the liquid diluent vaporize to generate the vaporized diluent. 9. The method of claim 6, wherein equilibrating the respective temperatures comprises heating and reducing the pressure of the discharged stream such that a temperature difference of less than about 1° F. exists between the polymer fluff and the vaporized diluent, and the polymer fluff and any remaining liquid diluent have respective temperatures within approximately 5° F. of a volatilization temperature of the liquid diluent at an exit of the flashline heater. 10. The method of claim 6, wherein equilibrating the respective temperatures comprises heating and reducing the pressure of the discharged stream such that the polymer fluff, the vaporized diluent, and any remaining liquid diluent have respective temperatures within approximately 1° F. of the volatilization temperature of the liquid diluent at the exit of the flashline heater. 11. The method of claim 6, comprising vaporizing substantially all of the second part of the liquid diluent within the flashline heater. 12. The method of claim 6, wherein a total travel time of the discharged stream through the flashline heater is at least approximately 8 seconds. 13. The method of claim 6, wherein heating the discharged stream in the flashline heater comprises using a first plurality of heat-variable sections to increase a temperature of the discharged stream, and substantially maintaining the temperature of the discharged stream in the flashline heater using a second plurality of heat-variable sections. 14. The method of claim 13, wherein a first set of the second plurality of heat-variable sections are interleaved with the first plurality of heat-variable sections. 15. The method of claim 14, wherein a second set of the second plurality of heat-variable sections are downstream from the first plurality of heat-variable sections. 16. The method of claim 6, wherein receiving the discharged stream in the flashline heater comprises continuously discharging the discharged stream from a polymerization reactor into the flashline heater. 17. A method, comprising: polymerizing an olefin monomer in a liquid diluent using an olefin polymerization catalyst to generate a polymer slurry, the polymer slurry comprising polymer fluff and the liquid diluent;continuously discharging the polymer slurry into a flashline heater;volatilizing, within the flashline heater, a first part of the liquid diluent and at least a portion of a second part of the liquid diluent of the discharged polymer slurry to generate vaporized diluent, wherein the first part is not entrained within the polymer fluff and the second part is entrained within the polymer fluff; anddischarging the vaporized diluent, any remaining second part of the diluent, and the polymer fluff from the flashline heater at thermal equilibrium. 18. The method of claim 17, comprising vaporizing substantially all of the first portion of the liquid diluent at least approximately 2.5 seconds before exiting the flashline heater. 19. The method of claim 17, wherein volatilizing, within the flashline heater, the first part of the diluent and at least the portion of the second part of the diluent comprises heating and reducing the pressure of the discharged stream such that the polymer fluff and any remaining liquid diluent have respective temperatures within approximately 5° F. of a volatilization temperature of the liquid diluent at the exit of the flashline heater. 20. The method of claim 17, comprising vaporizing substantially all of the second part of the liquid diluent within the flashline heater. 21. The method of claim 17, wherein volatilizing, within the flashline heater, the first part of the liquid diluent and at least the portion of the second part of the liquid diluent comprises heating the discharged polymer slurry using a first plurality of heat-variable sections to increase a temperature of the discharged polymer slurry, and substantially maintaining the temperature of the discharged polymer slurry in the flashline heater using a second plurality of heat-variable sections. 22. The method of claim 17, comprising receiving the vaporized diluent and the polymer fluff in a separation vessel from the flashline heater, separating the vaporized diluent from the polymer fluff in the separation vessel, discharging at least a portion of the polymer fluff from the separation vessel into a conduit, and providing additional heat to the portion of the polymer fluff within the conduit.