Method and apparatus for argon recovery in a cryogenic air separation unit integrated with a pressure swing adsorption system

Patent metadata

Field	Value
Publication number	US-10012438-B2
Application number	US-201615057148-A
Country	US
Kind code	B2
Filing date	Mar 1, 2016
Priority date	Jul 31, 2015
Publication date	Jul 3, 2018
Grant date	Jul 3, 2018

Abstract

A method and apparatus for argon recovery in which an impure argon stream is separated from air within a cryogenic air separation unit having a divided wall argon rejection/rectification column. The resulting argon stream is subsequently recovered and purified within an integrated pressure swing adsorption system to produce product grade argon.

First claim

What is claimed is:

1. A method of producing a purified argon product in a cryogenic air separation unit integrated with a pressure swing adsorption system, the method comprising the steps of:
separating argon from an oxygen-argon containing stream within a lower pressure column of the cryogenic air separation unit using an argon rectification column arrangement disposed within the lower pressure column, the separation of the argon from the oxygen-argon containing stream producing an impure argon stream having between about and 4% and 25% of oxygen impurities;
warming the impure argon stream to a temperature between about 200K and 300K in an argon recovery heat exchanger against a purified argon stream, a waste gas stream, and a stream of purified, compressed air;
pressurizing the warmed impure argon stream;
purifying the warmed, pressurized impure argon stream by introducing the warmed, pressurized impure argon stream into the pressure swing adsorption system, the pressure swing adsorption system comprising an adsorbent bed having an adsorbent configured for adsorbing the oxygen impurities to produce the purified argon stream and the waste gas stream, wherein the adsorbent bed is subjected to an alternating cycle having an on-line phase where the impure argon stream is purified within the adsorbent bed to produce the purified argon stream, and an off-line phase where the adsorbent contained in the adsorbent bed is regenerated and produces the waste gas stream; and
recycling the waste gas stream from the pressure swing adsorption system back to the argon rectification column arrangement disposed within the lower pressure column;
wherein the argon rectification column arrangement comprises a partition wall having a top section, a bottom section, a first surface, and a second surface opposite the first surface, the partition wall disposed within an outer shell of the lower pressure column; a plurality of mass transfer elements disposed adjacent to the first surface of the partitioned wall; an inlet disposed proximate the bottom section of the partition wall for receiving an ascending argon-oxygen containing vapor stream; an outlet disposed proximate the top section of the partition wall for withdrawing an ascending argon-rich vapor; an inlet disposed proximate the top section of the partition wall for receiving a down-flowing liquid reflux stream; an outlet disposed proximate the bottom section of the partition wall for withdrawing a descending oxygen rich liquid stream; and
wherein the impure argon stream is an argon vapor stream comprised of at least a portion of the ascending argon-rich vapor exiting the argon rectification column.

2. The method of claim 1 , wherein an argon condensing assembly is disposed within the lower pressure column at a location above the argon rectification column, the argon condensing assembly configured to condense another portion of the ascending argon-rich vapor against a sub-cooled bottoms liquid from the higher pressure column to produce a liquid argon stream.

3. The method of claim 2 , wherein at least a portion of the liquid argon stream from the argon condensing assembly is the down-flowing liquid reflux stream in the argon rectification column.

4. The method of claim 1 , wherein the adsorbent comprises carbon molecular sieves.

5. The method of claim 1 wherein the adsorbent comprises an ion-exchanged zeolite.

6. An apparatus for producing a purified argon product comprising:
a cryogenic air separation unit having a higher pressure column and a lower pressure column, and an argon rectification column arrangement disposed within the lower pressure column, the cryogenic air separation unit configured to produce an impure argon stream having between about and 4% and 25% of oxygen impurities from an oxygen-argon containing stream introduced from the lower pressure column to the argon rectification column arrangement;
an argon recovery heat exchanger configured to warm the impure argon stream against a purified argon, a waste gas stream, and a compressed and purified air stream;
an argon compressor or pump configured for pressurizing the warmed impure argon stream;
a pressure swing adsorption system configured for purifying the warmed, pressurized impure argon stream to the purified argon product by introducing the warmed, pressurized impure argon stream, the pressure swing adsorption system comprising an adsorbent bed having an adsorbent configured for adsorbing the oxygen impurities to produce a purified argon stream and the waste gas stream, wherein the adsorbent bed is subjected to an alternating cycle having an on-line phase where the impure argon stream is purified within the adsorbent bed to produce the purified argon stream, and an off-line phase where the adsorbent contained in the adsorbent bed is regenerated and produces the waste gas stream; and
a recycle conduit disposed between the pressure swing adsorption system and the argon rectification column arrangement and configured for recycling the waste gas stream from the pressure swing adsorption system to the argon rectification column arrangement disposed within the lower pressure column;
wherein the argon rectification column arrangement comprises a partition wall having a top section, a bottom section, a first surface, and a second surface opposite the first surface, the partition wall disposed within an outer shell of the lower pressure column; a plurality of mass transfer elements disposed adjacent to the first surface of the partitioned wall; an inlet disposed proximate the bottom section of the partition wall configured for receiving an ascending argon-oxygen containing vapor stream; an outlet disposed proximate the top section of the partition wall configured for withdrawing an ascending argon-rich vapor; an inlet disposed proximate the top section of the partition wall configured for receiving a down-flowing liquid reflux stream; an outlet disposed proximate the bottom section of the partition wall configured for withdrawing a descending oxygen rich liquid stream; and
wherein the impure argon stream is an argon vapor stream comprised of at least a portion of the ascending argon-rich vapor exiting the argon rectification column arrangement.

7. The apparatus of claim 6 , further comprising an argon condensing assembly disposed within the lower pressure column at a location above the argon rectification column arrangement and configured to condense another portion of the ascending argon-rich vapor from the argon rectification column arrangement against a sub-cooled bottoms liquid from the higher pressure column to produce a liquid argon stream.

8. The apparatus of claim 7 , wherein at least a portion of the liquid argon stream from the argon condensing assembly is the down-flowing liquid reflux stream in the argon rectification column arrangement.

9. The apparatus of claim 6 , wherein the adsorbent comprises carbon molecular sieves.

10. The apparatus of claim 6 , wherein the adsorbent comprises an ion-exchanged zeolite.

Assignees

• Du Hai
• Prosser Neil M
• Luo Yang
• Stephenson Neil A
• Praxair Technology Inc

Inventors

• Du Hai
• Prosser Neil M
• Luo Yang
• Stephenson Neil A

Classifications

• F25J3/04096

  of argon or argon enriched stream · CPC title

• F25J3/04678

  cooled by oxygen enriched liquid from high pressure column bottoms · CPC title

• F25J3/04103

  using solely hydrostatic liquid head · CPC title

• F25J2290/34

  Details about subcooling of liquids · CPC title

• F25J3/04296

  Claude expansion, i.e. expanded into the main or high pressure column · CPC title