Process for removing hydrocarbons from polymer slurries

Claim 2

A process for removing a hydrocarbon from a polymer slurry comprising the steps of: feeding a hydrocarbon-containing polymer slurry to a flash tank operated at a pressure sufficiently above atmospheric pressure, in the approximate range of about 70-120 psig, to flash at least about 80% of the hydrocarbon from the slurry; feeding the resulting slurry from the flash tank to a fluid bed dryer operated at a pressure in the approximate range of about 1-2 psig; stripping additional hydrocarbon from the polymer in the fluid bed dryer utilizing heated hydrocarbon as the stripping gas; transferring the resulting polymer from the fluid bed dryer to a powder silo wherein additional hydrocarbon is removed from the polymer utilizing a heated purge gas flowing countercurrent to the polymer; venting the hydrocarbon flashed from the slurry in the flash tank and recovering a major portion of said hydrocarbon in a cooling water condenser; and collecting from the powder silo polymer powder having a hydrocarbon content below about 100 ppm.

Claim 3

The process of claim 1 wherein said hydrocarbon is solvent or monomer.

Claim 4

The process of claim 2 wherein said hydrocarbon is a solvent and said polymer slurry is a polyolefin slurry.

Claim 5

The process of claim 3 wherein said solvent is isobutane and said polyolefin slurry is a polyethylene slurry.

Claim 6

The process of claim 4 wherein the powder collected from the powder silo is polyethylene powder which is substantially free of isobutane solvent.

Claim 7

The process of claim 5 further comprising venting from the powder silo the purge gas containing the hydrocarbon removed from the polymer.

Claim 8

The process of claim 5 further comprising recycling a portion of the isobutane output from the fluid bed dryer as the stripping gas in the fluid bed dryer and recovering a portion of the isobutane in a cooling water condenser.

Claim 9

The process of claim 5 wherein the collected polyethylene powder contains between about 50-100 ppm isobutane solvent.

Claim 10

The process of claim 4 wherein said flash tank is operated at a temperature in the range of about 110°-135° F.

Claim 11

The process of claim 9 wherein the slurry has a residence time in said flash tank of about 15 minutes.

Claim 12

The process of claim 10 wherein the stripping gas utilized in the fluid bed dryer is isobutane gas heated to about 220° F.

Claim 13

The process of claim 11 wherein the polyethylene has a residence time in said fluid bed dryer in the range of about 7-15 minutes.

Claim 14

The process of claim 12 wherein the purge gas utilized in the powder silo is nitrogen heated to about 180°-220° F.

Claim 15

The process of claim 13 wherein the polyethylene powder has a residence time in the powder silo of about 30 minutes.

Claim 16

A process for removing a hydrocarbon from a polymer slurry comprising the steps of: feeding a hydrocarbon-containing polymer slurry to a flash tank operated at a pressure sufficiently above atmospheric pressure, in the range of about 70-120 psig and at a temperature in the range of about 110°-135° F., to flash at least about 80% of the hydrocarbon from the slurry; feeding the resulting slurry from a flash tank to a fluid bed dryer operated at a pressure of about 1-2 psig; stripping additional hydrocarbon from the polymer in the fluid bed dryer utilizing heated hydrocarbon as the stripping gas; transferring the resulting polymer from the fluid bed dryer to a powder silo wherein additional hydrocarbon is removed from the polymer utilizing a heated purge gas flowing countercurrent to the polymer; venting the hydrocarbon flashed from the slurry in the flash tank and recovering a major portion of said hydrocarbon in a cooling water condenser; and collecting from the powder silo polymer powder having a hydrocarbon content below about 100 ppm.

Claim 17

A process for removing a hydrocarbon from a polymer slurry comprising the steps of: feeding a hydrocarbon-containing polymer slurry to a flash tank operated at a pressure sufficiently above atmospheric pressure, in the range of about 70-120 psig and at a temperature in the range of about 110°-135° F., to flash at least about 80% of the hydrocarbon from the slurry; feeding the resulting slurry from a flash tank to a fluid bed dryer operated at a pressure of about 1-2 psig; stripping additional hydrocarbon from the polymer in the fluid bed dryer utilizing heated hydrocarbon as the stripping gas; transferring the resulting polymer from the fluid bed dryer to a powder silo wherein additional hydrocarbon is removed from the polymer utilizing a heated purge gas flowing countercurrent to the polymer; venting the hydrocarbon flashed from the slurry in the flash tank and recovering a major portion of said hydrocarbon in a cooling water condenser; and collecting from the powder silo polymer powder having a hydrocarbon content below about 100 ppm.