Method for regenerating a pre-purification vessel

Patent metadata

Field	Value
Publication number	US-11619442-B2
Application number	US-202117234100-A
Country	US
Kind code	B2
Filing date	Apr 19, 2021
Priority date	Apr 19, 2021
Publication date	Apr 4, 2023
Grant date	Apr 4, 2023

Abstract

A system and method of regenerating a pre-purification vessel is provided that is particularly suitable for pre-purification of a feed air stream in cryogenic air separation unit that uses an oxygen-enriched purge gas stream for regeneration of the pre-purification unit. The disclosed pre-purification systems and methods are configured to remove substantially all of the water, carbon dioxide and other impurities from a feed air stream, optionally including hydrogen and carbon monoxide impurities. The method of regenerating a pre-purification vessel preferably involves regenerating the pre-purification vessel with an oxygen-enriched purge gas after depressurization of the vessel and thereafter partially repressurizing the pre-purification vessel with an auxiliary purge gas thereby diluting the oxygen concentration of the gases contained in the pre-purification vessel and optionally depressurizing the partially repressurized vessel.

First claim

What is claimed is:

1. A method of regenerating a pre-purification vessel, comprising the steps of:
(i) depressurizing a pre-purification vessel to a regeneration pressure, the pre-purification vessel having one or more layers of adsorbent and/or layers of catalyst disposed therein;
(ii) heating the one or more layers of adsorbent materials and/or one or more layers of catalyst materials disposed within the pre-purification vessel with an oxygen-enriched purge gas to desorb the water and carbon dioxide from the one or more layers;
(iii) cooling the one or more layers of adsorbent and/or layers of catalyst within the pre-purification vessel with another oxygen-enriched purge gas;
(iv) partially repressurizing the pre-purification vessel with an auxiliary purge gas to dilute the oxygen concentration of the gases contained in the pre-purification vessel after the cooling step;
(v) fully repressurizing the pre-purification vessel to an operating pressure for pre-purification of a feed gas, wherein the oxygen concentration of the gases in the repressurized pre-purification vessel is less than or equal to 30% by molar volume.

2. The method of claim 1 wherein the oxygen concentration of the gases in the repressurized pre-purification vessel is less than or equal to 26% by molar volume.

3. The method of claim 1 wherein the step of partially repressurizing the pre-purification vessel with the auxiliary purge gas further comprises partially repressurizing the pre-purification vessel to an intermediate pressure with the auxiliary purge gas; and thereafter depressurizing the pre-purification vessel and releasing the auxiliary purge gas and any oxygen-enriched purge gas retained within the pre-purification vessel.

4. The method of claim 1 wherein the step of partially repressurizing the pre-purification vessel with the auxiliary purge gas further comprises partially repressurizing the pre-purification vessel to an intermediate pressure with a nitrogen-rich gas having a nitrogen concentration above 85% by molar volume thereby diluting the oxygen concentration of gases retained in the pre-purification vessel.

5. The method of claim 1 wherein the oxygen-enriched purge gas has a temperature of at least 150° C.

6. The method of claim 1 wherein the another oxygen-enriched purge gas has a temperature of at less than or equal to 50° C.

7. The method of claim 1 wherein the pre-purification vessel is coupled to an air separation unit and the feed gas is air, wherein the one or more layers of adsorbent within the pre-purification vessels comprise activated alumina, silica gel, zeolite based molecular sieve, an X-type zeolite or combinations thereof and are configured to remove impurities, including water, carbon dioxide and other contaminants in the feed gas.

8. The method of claim 7 wherein the one or more layers of catalysts within the pre-purification vessels comprise hopcalite or noble metal catalysts and are configured to remove impurities, including hydrogen and carbon monoxide.

9. The method of claim 1 wherein the pre-purification vessel is coupled to an air separation unit and the oxygen-enriched purge gas and the another oxygen-enriched purge gas are taken from an oxygen-enriched stream from a distillation column system of the air separation unit.

10. The method of claim 9 wherein the step of heating the one or more layers of adsorbent materials and/or one or more layers of catalyst materials with the oxygen-enriched purge gas further comprises heating the oxygen-enriched stream using an electric, gas-fired or steam heater.

11. The method of claim 1 wherein the pre-purification vessel is coupled to an argon producing air separation unit and the oxygen-enriched purge gas and the the another oxygen-enriched purge gas are oxygen-enriched streams taken from an argon condenser associated with the argon producing air separation unit.

12. The method of claim 3 wherein the regeneration pressure is less than 6.0 bar; the operating pressure is greater than or equal to 6.0 bar; and the intermediate pressure is between the regeneration pressure and the operating pressure.

13. The method of claim 3 wherein the pre-purification vessel is coupled to an air separation unit and the auxiliary purge gas further comprises a dry air stream taken from a location downstream of the pre-purifier vessel associated with the air separation unit, or a diverted portion of feed air taken from a location upstream of the pre-purifier unit associated with the air separation unit, or a synthetic air stream taken from the air separation unit.

14. The method of claim 3 wherein the auxiliary purge gas is introduced to the pre-purification vessel via an auxiliary purge control valve and the release of the auxiliary purge gas and any retained gases from the pre-purification vessel during depressurization occurs via a partial depressurization control valve or the depressurization control valve.

15. The method of claim 4 wherein the pre-purification vessel is coupled to an air separation unit and the nitrogen-rich stream is taken from the air separation unit or a nitrogen storage tank.

16. The method of claim 4 wherein nitrogen-rich gas is introduced to the pre-purification vessel via an auxiliary purge gas control valve.

17. The method of claim 4 wherein the regeneration pressure is less than 6.0 bar; the operating pressure is greater than or equal to 6.0 bar; and the intermediate pressure is between the regeneration pressure and the operating pressure.

Assignees

• Handley James R
• Cyganovich Richard C
• Celik Cem E
• Powell Brian S
• Dasani Devang Ashok
• Praxair Technology Inc

Inventors

• Handley James R
• Cyganovich Richard C
• Celik Cem E
• Powell Brian S
• Dasani Devang Ashok

Classifications

• F25J3/04854

  Safety aspects of operation · CPC title

• B01D2255/20761

  Copper · CPC title

• F25J2245/42

  the recycled stream being nitrogen · CPC title

• B01D53/864

  Removing carbon monoxide or hydrocarbons · CPC title

• F25J3/04181

  Regenerating the adsorbents · CPC title