Method for the production of air gases by the cryogenic separation of air with improved front end purification and air compression

Patent metadata

Field	Value
Publication number	US-10895417-B2
Application number	US-201715468926-A
Country	US
Kind code	B2
Filing date	Mar 24, 2017
Priority date	Mar 25, 2016
Publication date	Jan 19, 2021
Grant date	Jan 19, 2021

Abstract

A method and apparatus for the production of air gases by the cryogenic separation of air with front end purification and air compression can include using an available compressed dry gas such as nitrogen, oxygen, stored purified air, or synthetic air to repressurize the adsorber without diverting any of the purified air just exiting the currently on-line adsorber or changing the flow rate of the main air compressor or air sent to the cold box. This enables the main air compressor (MAC) to operate at a relatively constant flow rate while also sending a relatively constant air flow to the cold box during this repressurization step, thereby reducing the risks of process upsets and minimizing capital expenditures related to the MAC and other warm-end equipments.

First claim

We claim:

1. A method for the production of air gases by the cryogenic separation of air with front end purification and air compression, the method comprising the steps of:
a) compressing atmospheric air to a pressure suitable for the cryogenic rectification of air to produce a compressed wet air stream;
b) purifying the compressed wet air stream of water and carbon dioxide within a front end purification system to produce a dry air stream having reduced amounts of water and carbon dioxide as compared to the compressed wet air stream, wherein the front end purification system comprises a first vessel and a second vessel configured in a permutable fashion, wherein the first vessel comprises a first adsorber and the second vessel comprises a second adsorber, wherein the first and second adsorbers operate in alternating cycles such that while the first adsorber is in an adsorption cycle, the second adsorber is in a regeneration cycle and while the second adsorber is in the adsorption cycle, the first adsorber is in the regeneration cycle;
c) introducing the dry air stream to a cold box under conditions effective to separate the dry air stream into a nitrogen enriched stream and an oxygen enriched stream; and
d) withdrawing the nitrogen enriched stream and the oxygen enriched stream from the cold box;
wherein the regeneration cycle for each of the first and the second vessels of the front end purification system further includes the steps of:
1) depressurizing the first or second vessel from an adsorption pressure to a regeneration pressure that is sufficiently low to release water and carbon dioxide from a surface of an adsorbent material within the vessel;
2) regenerating the adsorbent material using a first dry gas; and
3) pressurizing the first or second vessel to the adsorption pressure using a second gas,
wherein the second gas used in step 3) of the regeneration cycle is not sourced directly from the first or second vessel that is in the adsorption cycle,
wherein the flow rate of the dry air stream introduced to the cold box remains substantially constant during step c).

2. The method as claimed in claim 1 , wherein step 2) of the regeneration cycle for each vessel of the front end purification system further includes the steps of 2a) heating the adsorbent material to a regeneration temperature T R by heating the dry gas upstream the vessel for a first period of time and then 2b) cooling the adsorbent material to a second temperature T 2 by continuing to introduce the dry gas into the vessel, but without adding heat to the dry gas upstream of the vessel.

3. The method as claimed in claim 1 , wherein the flow rate of the compressed wet air stream sent to the front end purification system remains substantially constant during steps b) and 3).

4. The method as claimed in claim 1 , wherein during the step of pressurizing the vessel, the method comprises an absence of the steps of:
increasing the flow rate of the compressed wet air stream sent to the front end purification system; and
decreasing the flow rate of the dry air stream introduced to the cold box.

5. The method as claimed in claim 1 , wherein the step 3) of the regeneration cycle comprises an absence of sending a portion of the dry air stream from the first vessel to the second vessel when the second vessel is pressurizing.

6. The method as claimed in claim 1 , wherein the first dry gas comprises the nitrogen enriched stream from the cold box.

7. The method as claimed in claim 1 , wherein the second gas is a second dry gas.

8. The method as claimed in claim 7 , wherein the second dry gas comprises the nitrogen enriched stream from the cold box.

9. The method as claimed in claim 7 , wherein the second dry gas comprises a dry gas stream from an external source.

10. The method as claimed in claim 7 , wherein the second dry gas is a synthetic airstream consisting essentially of oxygen and nitrogen sourced from the cold box.

11. The method as claimed in claim 7 , wherein the second dry gas comprises nitrogen and oxygen, wherein the nitrogen content is between 70 and 88% and the oxygen content is between 12 and 30%.

12. The method as claimed in claim 7 , wherein the second dry gas is sourced from a compressed air storage tank, wherein the compressed air storage tank is in fluid communication with the front end purification system, such that the compressed air storage tank is configured to receive a portion of the dry air stream exiting the front end purification system prior to the dry air stream being introduced to the cold box.

13. The method as claimed in claim 1 , wherein the method further comprises a switch over step following step 3) of the regeneration cycle in which both the first adsorber and the second adsorber are adsorbing in a parallel fashion.

14. The method as claimed in claim 13 , wherein during the course of the switch over step, flow of the compressed wet air stream is gradually increased to the first or second adsorber that just finished pressurizing.

15. The method as claimed in claim 14 , wherein the rate of increasing the flow of the compressed wet air stream to the first or second adsorber that just finished pressurizing is adjusted based on the composition of the dry gas sent to the cold box or the composition of the dry gas exiting the first vessel and/or the second vessel or the composition of the second gas.

16. The method as claimed in claim 1 , further comprising the step of monitoring the composition of the purified gas at a location selected from within the front end purification system or between the front end purification system and the cold box.

17. A method for the production of air gases by the cryogenic separation of air, the method comprising the steps of:
compressing atmospheric air in a main air compressor to a pressure suitable for the cryogenic rectification of air to produce a compressed wet air stream;
purifying the compressed wet air stream of water and carbon dioxide within a front end purification system to produce a dry air stream having reduced amounts of water and carbon dioxide as compared to the compressed wet air stream;
introducing the dry air stream to a cold box under conditions effective to separate the dry air stream into a nitrogen enriched stream and an oxygen enriched stream; and
withdrawing the nitrogen enriched stream and the oxygen enriched stream from the cold box;
wherein the front end purification system comprises a first vessel and a second vessel configured in a permutable fashion such that while the first vessel is in an adsorption cycle, the second vessel is in a regeneration cycle,
wherein during the adsorption cycle of the first vessel, the first vessel receives the compressed wet air stream and produces the dry air stream;
wherein during the regeneration cycle, the second vessel is:
(a) depressurized from an adsorption pressure to a regeneration pressure that is sufficiently low to release water and carbon dioxide from a surface of an adsorbent material within the second vessel;
(b) regenerated by flowing a first dry gas across the adsorbent material of the second vessel to remove released water and carbon dioxide; and
(c) repressurized to the adsorption pressure using a second gas,

wherein the second vessel is repressurized during step (c) without:
(1) diverting any of the dry air stream exiting the first vessel to the second vessel,
(2) changing the flow rate of atmospheric air being compressed in the main air compressor, or
(3) changing the flow rate of the dry air stream sent to the cold box.

Assignees

• Air Liquide

Inventors

• Kong Paul
• Pham-Huy Minh
• Yip Wendy

Classifications

• Y02C20/40

  of CO2 · CPC title

• F25J2205/72

  Pressurising or depressurising the adsorption vessel · CPC title

• F25J3/04775

  Air purification and pre-cooling · CPC title

• F25J2245/40

  the recycled stream being air · CPC title

• F25J2210/40

  Air or oxygen enriched air, i.e. generally less than 30mol% of O2 · CPC title