Process for purifying recirculating gases of condensed polymer particles

Claim 2

A process for eliminating low molecular-weight polymers from recirculting gases of facilities carrying out polymerization or copolymerization of ethylene at a pressure of 300 to 2500 bars and a temperature of 130° C. to 350° C., in which facilities a mixture of monomer and polymer leaving the reactor is expanded into a separator operating under a pressure of 50 to 500 bars, said gases being the gaseous phase leaving said separator, comprising (a) passing said gases, at a temperature at least 20° C. higher than the melting point of the low polymers, through at least one standard cyclone at an inlet velocity between 1 and 10 m/s to eliminate some of said low polymers; (b) then cooling said gases from said cyclone to a temperature lower than the melting point of the low polymers; and (c) then passing said cooled gases through at least one heated cyclone at an inlet velocity between 2 and 20 m/s to eliminate more of said low polymers.

Claim 3

The process of claim 1, wherein the standard cyclone is located inside a pressure-resistant vessel.

Claim 4

The process of claim 1, wherein the heated cyclone is designed to resist a pressure of 50 to 500 bars.

Claim 5

The process of claim 1, further comprising, after passage of the recirculating gases through a standard cyclone and before cooling, passing said gases through a coalescing means capable of coalescing liquid polymer particles having a dimension smaller than or equal to 5μ.

Claim 6

The process of claim 4, further comprising, after the passage of the recirculating gases through a coalescing means and before cooling, passing said recirculating gases through a standard cyclone at an inlet velocity of 1 to 10 m/s.

Claim 7

The process of claim 4, wherein the coalescing means is constituted of stainless steel having a porosity between 0.2 and 1.0.

Claim 8

The process of claim 5, further comprising collecting low polymers separated from said gases in said coalescing means or said cyclones in at least one decanter, and injecting said collected polymers into a polymer line of said facilities at a pressure lower than that of said separator.

Claim 9

A process for eliminating low molecular-weight polymers from recirculating gases of facilites carrying out polymerization or copolymerization of ethylene at a pressure of 300 to 2500 bars and a temperature of 130° C. to 350° C., in which facilities a mixture of monomer and polymer leaving the reactor is expanded into a separator operating under a pressure of 50 to 500 bars, said gases being the gaseous phase leaving said separator, comprising (a) passing said gases, at a temperature at least 20° C. higher than the melting point of the low polymers, through at least one standard cyclone at an inlet velocity between 1 and 10 m/s to eliminate some of said low polymers; (b) then cooling said gases from said cyclone to a temperature lower than the melting point of the low polymers; (c) then passing said cooled gases through at least one heated cyclone at an inlet velocity between 2 and 20 m/s to eliminate more of said low polymers; (d) collecting low polymers separated from said gases in at least one decanter; and (e) injecting said collected polymers into a polymer line of said facilities at a pressure lower than that of said separator.

Claim 10

A process for eliminating low molecular-weight polymers from recirculating gases of facilites carrying out polymerization or copolymerization of ethylene at a pressure of 300 to 2500 bars and a temperature of 130° C. to 350° C., in which facilities a mixture of monomer and polymer leaving the reactor is expanded into a separator operating under a pressure of 50 to 500 bars, said gases being the gaseous phase leaving said separator, comprising (a) passing said gases, at a temperature at least 20° C. higher than the melting point of the low polymers, through at least one standard cyclone at an inlet velocity between 1 and 10 m/s to eliminate some of said low polymers; (b) then cooling said gases from said cyclone to a temperature lower than the melting point of the low polymers; (c) then passing said cooled gases through at least one heated cyclone at an inlet velocity between 2 and 20 m/s to eliminate more of said low polymers; (d) collecting low polymers separated from said gases in at least one decanter; and (e) injecting said collected polymers into a polymer line of said facilities at a pressure lower than that of said separator.