Nitrogen conservation in polymerization processes

Patent metadata

Field	Value
Publication number	US-11623176-B2
Application number	US-202016902856-A
Country	US
Kind code	B2
Filing date	Jun 16, 2020
Priority date	May 7, 2018
Publication date	Apr 11, 2023
Grant date	Apr 11, 2023

Abstract

A closed-loop nitrogen transport system including a first transfer line configured for nitrogen pressure conveyance of a polymer fluff from at least one upstream vessel to at least one downstream vessel, a second transfer line configured to return a nitrogen gas stream comprising primarily nitrogen from the at least one downstream vessel to the at least one upstream vessel, a conveyor blower operable to provide flow throughout the closed loop, and a treatment unit operable to remove hydrocarbons from at least a portion of the nitrogen gas stream comprising primarily nitrogen, to provide a purified nitrogen stream.

First claim

We claim:

1. A closed-loop nitrogen transport system comprising:
a first transfer line configured for nitrogen pressure conveyance of a polymer fluff from at least one upstream vessel to at least one downstream vessel;
a second transfer line configured to return a nitrogen gas stream comprising primarily nitrogen from the at least one downstream vessel to the at least one upstream vessel;
a conveyor blower operable to provide flow throughout the closed loop; and
a treatment unit operable to remove hydrocarbons from at least a portion of the nitrogen gas stream comprising primarily nitrogen, to provide a purified nitrogen stream.

2. The closed-loop nitrogen transport system of claim 1 further comprising a spillback line configured to remove the at least a portion of the nitrogen gas stream from the second transfer line and introduce same into the treatment unit, and a purified nitrogen return line configured to introduce the purified nitrogen stream into the second transfer line.

3. The closed-loop nitrogen transport system of claim 1 , wherein the conveyor blower is on the second transfer line, wherein the spillback line is downstream of the conveyor blower, wherein the purified nitrogen return line is configured to introduce the purified nitrogen stream into the second transfer line upstream of the conveyor blower, or a combination thereof.

4. The closed-loop nitrogen transport system of claim 1 , wherein the treatment unit comprises an adsorbent bed, a membrane-based separation unit, a catalytic converter, a refrigeration unit, pressurized oil absorption unit, or a combination thereof, and/or wherein the at least one upstream vessel comprises a purge column downstream of one or more polymerization reactors and configured to separate a purge gas from a polymer fluff introduced thereto, and/or wherein the at least one downstream vessel comprises an extruder feed hopper, an extruder, a fluff storage vessel, or a combination thereof.

5. The closed-loop nitrogen transport system of claim 4 , wherein the treatment unit comprises the adsorbent bed, and wherein the adsorbent bed comprises a polymeric adsorbent, silica, activated charcoal, zeolite molecular sieve, or a combination thereof.

6. The closed-loop nitrogen transport system of claim 1 , wherein the treatment unit comprises a pressure swing adsorption (PSA) unit.

7. The closed-loop nitrogen transport system of claim 4 , wherein the at least one upstream vessel comprises the purge column, and further comprising an isobutane nitrogen recovery unit (INRU) fluidly connected with the purge column and configured to separate a nitrogen-containing gas from the purge gas to provide a side stream comprising recovered diluent and other hydrocarbons.

8. The closed-loop nitrogen transport system of claim 7 further comprising a line configured to introduce at least a portion of the nitrogen-containing gas, the side stream, or both from the INRU into the purge column, a line configured to introduce at least a portion of the nitrogen-containing gas, the side stream, or both from the INRU into the treatment unit, or a combination thereof.

9. A closed-loop nitrogen transport process comprising:
conveying, with nitrogen gas, a polymer fluff from at least one upstream vessel to at least one downstream vessel via a first transfer line;
utilizing a conveyor blower to return a nitrogen gas stream comprising primarily nitrogen from the at least one downstream vessel to the at least one upstream vessel via a second transfer line;
introducing at least a portion of the nitrogen gas stream comprising primarily nitrogen into a treatment unit operable to remove hydrocarbons therefrom and provide a purified nitrogen stream; and
introducing at least a portion of the purified nitrogen stream into the at least upstream vessel, the first transfer line, the second transfer line, or a combination thereof, whereby a concentration of hydrocarbons in the nitrogen gas stream comprising primarily nitrogen is maintained at a desired level.

10. The closed-loop nitrogen transport process of claim 9 , wherein the desired level is in the range of from 50 to 10,000 ppm hydrocarbons, and/or wherein the treatment unit comprises an adsorbent bed, a membrane-based separation unit, a catalytic converter, high pressure oil absorption unit, a refrigeration unit or a combination thereof.

11. The closed-loop nitrogen transport process of claim 10 , wherein the treatment unit comprises the adsorbent bed, and wherein the adsorbent bed comprises a polymeric adsorbent, silica, activated charcoal, or a combination thereof.

12. The closed-loop nitrogen transport process of claim 9 , wherein the treatment unit comprises a pressure swing adsorption (PSA) unit.

13. The closed-loop nitrogen transport process of claim 9 , wherein the at least one upstream vessel comprises a purge column configured to separate a purge gas from a polymer fluff introduced thereto, and/or wherein the at least one downstream vessel comprises an extruder feed hopper, an extruder, a fluff storage vessel, or a combination thereof.

14. The closed-loop nitrogen transport process of claim 13 , wherein the at least one upstream vessel comprises the purge column, and further comprising separating a purge gas extracted from the purge column into a nitrogen-containing gas and an isobutane-containing gas.

15. The closed-loop nitrogen transport process of claim 14 further comprising introducing at least a portion of the nitrogen-containing gas into the purge column, introducing at least a portion of the nitrogen-containing gas, the isobutane-containing gas, or both into the treatment unit, or a combination thereof.

16. A method comprising:
contacting a nitrogen purge stream comprising a contaminant selected from hydrocarbons, carbon dioxide, water, ammonia, alcohols, acetylene, carbonyls, sulfur compounds, peroxides, ammonia, amines, phosphines, or combinations thereof with an adsorbent, a catalyst, or both to produce a treated nitrogen purge stream comprising a reduced amount of the contaminant,
wherein the nitrogen purge stream is produced in a polymerization process, and
wherein the nitrogen purge stream is a nitrogen purge of a closed-loop nitrogen transport system utilized to transfer a polymer fluff from an upstream vessel to a downstream vessel, wherein the nitrogen purge stream is a treater bed regeneration effluent stream produced during regeneration of a treater bed utilized to remove at least one impurity from a feed stream to a polymerization reactor, or a combination thereof.

17. The method of claim 16 , wherein the nitrogen purge stream is produced in an ethylene polymerization process.

18. The method of claim 16 , wherein the upstream vessel comprises a purge column configured to separate a purge gas from a polymer fluff introduced thereto; wherein the downstream vessel comprises an extruder feed hopper, an extruder, a fluff storage vessel, or a combination thereof; or both.

19. The method of claim 16 , wherein the adsorbent comprises silica gel, a polymeric adsorbent, activated charcoal, or a combination thereof; wherein the catalyst comprises a catalytic converter; or both.

20. The method of claim 18 , wherein the nitrogen purge stream is produced in an ethylene polymerization process, and
wherein the adsorbent comprises silica gel, a polymeric adsorbent, activated charcoal, or a combination thereof; wherein the catalyst comprises a catalytic converter; or both.

Assignees

• Chevron Phillips Chemical Co Lp

Inventors

• Ji Lei
• Hendrickson Gregory G
• Mcelvain Robert R
• Bridges Steven D
• Drew Jennifer F

Classifications

• B01D2253/106

  Silica or silicates · CPC title

• B01D2257/80

  Water · CPC title

• C08F10/02

  Ethene · CPC title

• B01D2257/502

  Carbon monoxide · CPC title

• B01D53/047 Primary

  Pressure swing adsorption · CPC title