Process for purging propane in a polypropylene manufacturing process

Patent metadata

Field	Value
Publication number	US-9120882-B2
Application number	US-201314374633-A
Country	US
Kind code	B2
Filing date	Jan 24, 2013
Priority date	Jan 26, 2012
Publication date	Sep 1, 2015
Grant date	Sep 1, 2015

Abstract

A process can include polymerizing propylene in a polymerization zone, withdrawing an effluent, and sending the effluent to a separation zone. A stream can be sent from the separation zone to a splitter to produce an overhead and a bottom stream. The overhead can be recycled to the polymerization zone, and the bottom stream can be sent to a membrane separation zone to produce a permeate and a purge. Optionally, the bottom stream can be washed in a scrubber, and an overhead of the scrubber can be sent to the membrane separation zone. The permeate can be recycled to the polymerization zone. A process can include providing a membrane separation zone to a polypropylene manufacturing facility that includes a polymerization zone, a separation zone, a splitter, and optionally a scrubber. The membrane separation zone can be fed a bottoms stream of the splitter or an overhead of the scrubber.

First claim

The invention claimed is:

1. A process comprising:
a) polymerizing propylene in a polymerization zone;
b) withdrawing from said polymerization zone an effluent comprising polypropylene, propylene, propane and optionally a solvent;
c) sending said effluent to a separation zone thereby producing polypropylene, optionally the solvent and a stream comprising propylene and propane;
d) optionally recycling the solvent to the polymerization zone;
e) sending said stream comprising propylene and propane to a splitter thereby producing an overhead consisting essentially of propylene recycled to the polymerization zone and a rich propane bottom stream comprising a minor part of propylene;
f) sending the rich propane bottom stream to a membrane separation zone thereby producing a permeate having an enhanced propylene content and a reduced propane content and a purge having an enhanced propane content and a reduced propylene content; and
g) recycling the permeate to the polymerization zone.

2. The process of claim 1 , wherein only a part of the rich propane bottom stream of the splitter is sent to the membrane separation zone, and wherein the remaining part of the rich propane bottom stream is purged or recycled to the polymerization zone.

3. The process of claim 1 , wherein from 20 to 100 percent of the rich propane bottom stream of the splitter is sent to the membrane separation zone, and wherein any remaining part of the rich propane bottom stream is purged or recycled to the polymerization zone.

4. The process of claim 1 , wherein the membrane separation zone comprise a membrane that exhibits a higher permeability for propylene than for propane.

5. The process of claim 1 , wherein the stream comprising propylene and propane comprises form 0.5 to 30 weight percent propane and from 1 to 40 weight percent of propylene.

6. The process of claim 1 , wherein the overhead of the splitter has a propylene content of at least 99.5 weight percent.

7. A process comprising:
a) polymerizing propylene in a polymerization zone;
b) withdrawing from said polymerization zone an effluent comprising polypropylene, propylene, propane and optionally a solvent;
c) sending said effluent to a separation zone thereby producing polypropylene, optionally the solvent and a stream comprising propylene and propane;
d) optionally recycling the solvent to the polymerization zone;
e) sending said stream comprising propylene and propane to a splitter thereby producing an overhead consisting essentially of propylene recycled to the polymerization zone and a rich propane bottom stream comprising a minor part of propylene;
f) washing the rich propane bottom stream produced in the splitter in a scrubber to remove contaminants and sending an overhead of said scrubber to a membrane separation zone, thereby producing a permeate having an enhanced propylene content and a reduced propane content and a purge having an enhanced propane content and a reduced propylene content; and
g) recycling the permeate to the polymerization zone.

8. The process according to claim 7 , wherein only a part of the overhead of the scrubber is sent to the membrane separation zone, and wherein the remaining part of the overhead of the scrubber is purged or recycled to the polymerization zone.

9. The process according to claim 7 , wherein only a part of the rich propane bottom stream produced in the splitter is washed in the scrubber to remove contaminants and the overhead of said scrubber is sent to the membrane separation zone, and wherein the remaining part of the rich propane bottom stream produced in the splitter is purged or recycled to the polymerization zone.

10. The process according to claim 7 , wherein from 20 to 100% of the rich propane bottom stream produced in the splitter is washed in the scrubber to remove contaminants and the overhead of said scrubber is sent to the membrane separation zone, and wherein any remaining part of the rich propane bottom stream produced in the splitter is purged or recycled to the polymerization zone.

11. A process comprising:
providing a membrane separation zone to a polypropylene manufacturing facility comprising:
a polymerization zone;
a separation zone to recover polypropylene, optionally a solvent and a stream comprising propylene and propane from the polymerization zone; and
a splitter to separate propane and propylene;
wherein:
the membrane separation zone is fed a bottoms stream of the splitter, thereby producing a purge and a permeate recycled to the polymerization zone; or
a scrubber is inserted between the bottoms of the splitter and the membrane separation zone to wash the bottoms stream of the splitter to remove contaminants, wherein the membrane separation zone is fed an overhead of the scrubber, thereby producing the purge and the permeate recycled to the polymerization zone.

12. The process of claim 11 , wherein the membrane separation zone is fed the bottoms stream of the splitter, thereby producing the purge and the permeate recycled to the polymerization zone.

13. The process of claim 12 , wherein only a part of the bottoms stream of the splitter is sent to the membrane separation zone, and wherein the remaining part of the bottoms stream of the splitter is purged or recycled to the polymerization zone.

14. The process of claim 11 , wherein the scrubber is inserted between the bottoms of the splitter and the membrane separation zone to wash the bottoms stream of the splitter to remove contaminants, wherein the membrane separation zone is fed the overhead of the scrubber, thereby producing the purge and the permeate recycled to the polymerization zone.

15. The process of claim 14 , wherein only a part of the overhead of the scrubber is sent to the membrane separation zone, the remaining part of the overhead of the scrubber is purged or recycled to the polymerization zone.

16. The process of claim 11 , wherein a part of the bottoms stream of the splitter is washed in the scrubber to remove contaminants and the overhead of said scrubber is sent to the membrane separation zone, and wherein the remaining part of the bottoms stream of the splitter is purged or recycled to the polymerization zone.

Assignees

• Total Res & Technology Feluy

Inventors

• Janssens Els
• Avaullee Laurent
• Richet Marc

Classifications

• C08F110/06 Primary

  Propene · CPC title

• C08L23/10

  Homopolymers or copolymers of propene · CPC title

• C08F6/001 Primary

  Removal of residual monomers by physical means · CPC title