Pressure swing adsorption process

• US 4,732,578 A
• Filed: 12/09/1986
• Issued: 03/22/1988
• Est. Priority Date: 12/09/1985
• Status: Expired due to Term

• Current Assignee: Linde AG (Linde Plc)
• Original Assignee: Linde AG (Linde Plc)
• Inventors: Benkmann, Christian
• Primary Examiner(s): SPITZER, ROBERT H
• Application Number:
  US06/939,911
• Time in Patent Office: 469 Days
• Field of Search: 55/21, 55/25, 55/26, 55/31, 55/33, 55/35, 55/58, 55/59, 55/62, 55/68, 55/74, 55/75, 55/160-163, 55/179, 55/387, 55/389
• US Class Current: 95/22
• CPC Class Codes: B01D 2256/10 Nitrogen
• CPC Class Codes: B01D 2256/16 Hydrogen
• CPC Class Codes: B01D 2257/102 Nitrogen
• CPC Class Codes: B01D 2257/504 Carbon dioxide
• CPC Class Codes: B01D 2259/40001 Methods relating to additional, e.g. intermediate, treatment of process gas
• CPC Class Codes: B01D 2259/40007 Controlling pressure or temperature swing adsorption
• CPC Class Codes: B01D 2259/40015 with two sub-steps
• CPC Class Codes: B01D 2259/40018 with more than three sub-steps
• CPC Class Codes: B01D 2259/4003 with two sub-steps
• CPC Class Codes: B01D 2259/40032 with three sub-steps
• CPC Class Codes: B01D 2259/40033 with more than three sub-steps
• CPC Class Codes: B01D 2259/40052 Recycled product or process gas
• CPC Class Codes: B01D 2259/403 using three beds
• CPC Class Codes: B01D 2259/4062 using six beds
• CPC Class Codes: B01D 53/047 Pressure swing adsorption
• CPC Class Codes: Y02C 20/40 of CO2

Abstract

A pressure swing adsorption process for the selective adsorption of at least one gaseous component from a gaseous mixture and an apparatus for performing the process wherein the gaseous mixture is conducted in cyclic alternation through at least three adsorbers and each adsorber is subdivided into two serially connected adsorber sections. The feed gas mixture is passed, during an adsorption phase, through respectively two series-connected adsorber sections. After termination of at least one cocurrent expansion phase, the adsorber sections are isolated from each other, and the first adsorber section, i.e., first traversed by the feed gas mixture, is further expanded while the second adsorber section is maintained at a higher pressure. Thereafter, the second adsorber section can be expanded countercurrently and thus-withdrawn countercurrent expansion gas can be utilized for purging the first adsorber section.

Claims

1. In a pressure swing adsorption process for the selective adsorption of at least one gaseous component from a feed gas mixture comprising conducting the mixture in cyclic alternation through at least three adsorbers, each of said at least three adsorbers passing through a switching cycle in staggered fashion with respect to one another, said switching cycle including (a) an adsorption phase wherein said feed gas mixture is introduced at an elevated inlet pressure into an adsorber, said at least one gaseous component is adsorbed, and unadsorbed product gas is withdrawn from the adsorber;

(b) a cocurrent expansion phase, after termination of said adsorption phase, during which the adsorber is regenerated by being depressurized to form an expansion gas which is passed on at least in part to other adsorbers for partial repressurization thereof; and

(c) a pressurization phase during which the adsorber is subsequently repressurized to said inlet pressure, the improvement comprising each of said adsorbers being divided into a first adsorber section and a second adsorber section, said first and second adsorber sections being connected in series, and during said adsorption phase said feed gas mixture being respectively conducted through said first and second adsorber sections, said adsorber sections being isolated from each other after said cocurrent expansion phase and said first adsorber section being subjected to further depressurization while said second adsorber section is maintained at a higher pressure.

2. A process according to claim 1, wherein said second adsorber section prior to said pressurization phase and after said further depressurization of said first adsorber section is depressurized in a countercurrent expansion phase to form a countercurrent expansion gas which is used to purge said first adsorber section.

3. A process according to claim 2, wherein during said countercurrent expansion phase the countercurrent expansion gas from said second adsorber section is expanded, by means of a regulating valve, into said first adsorber section after said further depressurization of the latter whereby it is conducted as purge gas through said first adsorber section.

4. A process according to claim 3, wherein during said countercurrent expansion phase the pressure of said second adsorber section is continuously measured and compared with a predetermined desired value and said regulating valve is adjusted in accordance with the measured pressure of said second adsorber section.

5. A process according to claim 4, wherein said second adsorber section is provided with a pressure monitoring means and said pressure monitoring means sends signals to a program control unit which controls the operation of said regulating valve.

6. A process according to claim 1, wherein said first and second adsorber sections are jointly depressurized during said cocurrent expansion phase.

7. A process according to claim 6, wherein during said further depressurization of the said first adsorber section the pressure of said second adsorber is substantially maintained at the final pressure of the joint cocurrent expansion phase.

8. A process according to claim 6, wherein during the joint cocurrent expansion phase both adsorber sections are depressurized to a pressure corresponding to about 0.5 to 1.0 times the partial pressure of the adsorbed component.

9. A process according to claim 6, wherein during the joint cocurrent expansion phase both adsorber sections are depressurized to a pressure corresponding to about 0.7 to 0.8 times the partial pressure of the adsorbed component.

10. A process according to claim 6, wherein during the joint cocurrent expansion phase said first and second adsorber sections, cocurrent expansion gas is withdrawn from both the outlet end of said first adsorber section and the outlet end of said second adsorber section and introduced, respectively, into the first and second adsorber sections of another adsorber.

11. A process according to claim 1, wherein said further depressurization of said first adsorber section is performed at least in part by a countercurrent expansion.

12. A process according to claim 1, wherein said inlet pressure of said feed gas mixture is about 10-100 bar.

13. A process according to claim 1, wherein said inlet pressure of said feed gas mixture is about 20-100 bar.

14. A process according to claim 1, wherein said inlet pressure of said feed gas mixture is about 30-90 bar.

15. A process according to claim 1, wherein the partial pressure of the adsorbed component in said second adsorber section is at least about twice the lowest process pressure and wherein said second adsorber section is regenerated solely by depressurization.

16. A process according to claim 1, wherein the lowest pressure experienced by each adsorber section is substantially the same.

17. A process according to claim 1, wherein the feed gas mixture contains at least about 30 mol-% of adsorbable components.

18. A process according to claim 1, wherein the feed gas mixture contains at least three different components having different adsorbability and at the end of said adsorption phase, in the first adsorber section, essentially only the component having the highest adsorbability is adsorbed, in the second adsorber section, essentially only the component of intermediate adsorbance is adsorbed, and the gas withdrawn from the second adsorber section is enriched with the least adsorbable component.

19. A process according to claim 18, wherein said first adsorber section during said further depressurization is initially depressurized in cocurrent mode and the resultant cocurrent expansion gas is introduced into another first adsorber section for repressurization thereof.

20. A process according to claim 18, wherein said first and second adsorber sections are jointly depressurized during said cocurrent expansion phase.

21. A process according to claim 20, wherein during the joint cocurrent expansion phase, both adsorber sections are depressurized to a pressure corresponding to about 0.5 to 1.0 times the partial pressure of that component of said at least three components which is present in the feed gas mixture at the highest concentration.

22. A process according to claim 20, wherein during the joint cocurrent expansion phase, both adsorber sections are depressurized to a pressure corresponding to about 0.7 to 0.8 times the partial pressure of that component of said at least three components which is present in the feed gas mixture at the highest concentration.

23. A process according to claim 18, wherein the feed gas mixture consists essentially of hydrogen and nitrogen in a proportion of below 3:

1 and, carbon dioxide and by adsorption of carbon dioxide and partial adsorption of nitrogen, a product gas is obtained essentially free of carbon dioxide and contains hydrogen and nitrogen in a proportion of about 3;

1.

24. A process according to claim 1, wherein during said pressurization phase said first adsorber section is isolated from said second adsorber section and said first adsorber section is then pressurized to an intermediate pressure with cocurrent expansion gas from another first adsorber section.

25. A process according to claim 24, wherein after said first section is brought to said intermediate pressure, cocurrent expansion gas from another adsorber is introduced only to said second adsorber section until the pressure of said second adsorber section is substantially equal to the intermediate pressure of said first adsorber section and thereafter connecting said first and second adsorber sections and further pressurizing said first and second adsorber sections jointly with cocurrent expansion gas from another adsorber.

26. A process according to claim 25, wherein connecting of the two adsorber sections to be pressurized is controlled by a program control unit which receives signals from pressure monitoring means associated with each adsorber section.

27. In an apparatus for conducting a pressure swing adsorption process comprising at least three adsorbers, each of said adsorbers being connected by means of valves to a feed gas supply conduit, a discharge conduit for unadsorbed gas, a residual gas conduit, and at least one pressure equalization conduit, and a program control unit for controlling the operation of said valves, the improvement wherein each adsorber is subdivided into a first adsorber section and a second adsorber, said first and second adsorber sections being connected in series, and a regulating valve is arranged between said first and second adsorber sections, the position of said regulating valve being controlled by said program control unit in dependence on signals sent to said program control unit from a pressure measuring means associated with said second adsorber section.

28. An apparatus according to claim 27, wherein said first adsorber section is also provided with a pressure measuring means.