Process for the purification of natural gas

• US 5,174,796 A
• Filed: 10/09/1991
• Issued: 12/29/1992
• Est. Priority Date: 10/09/1991
• Status: Expired due to Term

• Current Assignee: UOP Llc (Honeywell International Inc.)
• Original Assignee: UOP Llc (Honeywell International Inc.)
• Inventors: Patel, Kirit, Davis, Mark M., Gray, Robert L. Jr.
• Primary Examiner(s): SPITZER, ROBERT H
• Application Number:
  US07/774,020
• Time in Patent Office: 447 Days
• Field of Search: 55/25, 55/26, 55/31, 55/33, 55/58, 55/62, 55/68, 55/74, 55/75
• US Class Current: 95/100
• CPC Class Codes: B01D 2253/102 Carbon
• CPC Class Codes: B01D 2253/104 Alumina
• CPC Class Codes: B01D 2253/106 Silica or silicates
• CPC Class Codes: B01D 2256/245 Methane
• CPC Class Codes: B01D 2257/102 Nitrogen
• CPC Class Codes: B01D 2257/7025 Methane
• CPC Class Codes: B01D 2258/06 Polluted air
• CPC Class Codes: B01D 2259/40015 with two sub-steps
• CPC Class Codes: B01D 2259/4003 with two sub-steps
• CPC Class Codes: B01D 2259/40033 with more than three sub-steps
• CPC Class Codes: B01D 2259/40041 with more than three sub-steps
• CPC Class Codes: B01D 2259/40045 with two sub-steps
• CPC Class Codes: B01D 2259/40052 Recycled product or process gas
• CPC Class Codes: B01D 2259/40077 Direction of flow
• CPC Class Codes: B01D 2259/4061 using five beds
• CPC Class Codes: B01D 2259/4062 using six beds
• CPC Class Codes: B01D 2259/414 using different types of adsorbents
• CPC Class Codes: B01D 53/047 Pressure swing adsorption
• CPC Class Codes: Y02C 20/20 of methane

Abstract

A process is provided for the purification of natural gas wherein the nitrogen content of natural gas is reduced to pipeline specification using a pressure swing adsorption processes with a suitable selective adsorbent for methane purification. More specifically, the present invention relates to the use of a particular combination of steps in the PSA cycle to produce a product natural gas having a reduced nitrogen content, a nitrogen-rich stream and a high heat content fuel gas stream.

Claims

1. A pressure swing adsorption process for the reduction of the nitrogen content of a gas feedstream comprising methane and nitrogen said process comprising:

(a) passing said feedstream cocurrently through a first adsorption zone and contacting said feedstream with an adsorbent material in an adsorbent bed comprising said adsorbent material and void space to selectively adsorb methane on the adsorbent material and pressure the adsorption zone to a first pressure;

(b) discontinuing the passing of the feedstream to the first adsorption zone and partially depressurizing the adsorption zone to a second pressure by cocurrently withdrawing a first and a second nitrogen-rich gas stream from said first adsorption zone;

(c) countercurrently passing at least a portion of one of said nitrogen-rich gas streams to a second adsorption zone;

(d) venting at least a portion of one of said nitrogen-rich gas streams from the process;

(e) depressurizing said first adsorption zone to a third pressure that is lower than said second pressure by cocurrently withdrawing a high heat content fuel gas stream;

(f) countercurrently depressurizing the first adsorption zone and countercurrently recovering a first product gas stream from said first adsorption zone;

(g) countercurrently purging the first adsorption zone with a nitrogen-rich gas stream and countercurrently recovering a second product gas stream from said first adsorption zone;

(h) countercurrently repressurizing the adsorption zone by passing at least a portion of a third nitrogen-rich gas stream to said first adsorption zone; and

(i) countercurrently repressurizing the adsorption zone by passing at least a portion of a fourth nitrogen-rich stream to said first adsorption zone.

2. A pressure swing adsorption process for the reduction of the nitrogen content of a gas feedstream comprising methane and nitrogen said process comprising:

(a) passing said feedstream cocurrently through a first adsorption zone and contacting said feedstream with an adsorbent material in an adsorbent bed comprising said absorbent material and void space to selectively adsorb methane on the adsorbent material and pressure the adsorption zone to a first pressure;

(b) discontinuing the passing of the feedstream to the first adsorption zone and cocurrently passing at least a portion of a first product stream gas into said first adsorption zone to displace the nitrogen from the void space and to raise the pressure of said first adsorption zone to a second pressure;

(c) discontinuing the passing of the first product gas to said first adsorption zone and partially depressurizing the adsorption zone to a third pressure by cocurrently withdrawing a first and a second nitrogen-rich gas stream from said first adsorption zone;

(d) countercurrently passing at least a portion of one of said nitrogen-rich gas streams to a second adsorption zone;

(e) venting at least a portion of one of said nitrogen-rich gas streams from the process;

(f) depressurizing said first adsorption zone to a fourth pressure that is lower than said third pressure by cocurrently withdrawing a high heat content fuel gas stream;

(g) countercurrently depressurizing the first adsorption zone to a desorption pressure and countercurrently recovering a second product gas stream from said first adsorption zone;

(h) countercurrently purging the first adsorption zone with a nitrogen-rich gas stream and countercurrently recovering a third product gas stream from said first adsorption zone;

(i) countercurrently repressurizing the first adsorption zone by passing at least a portion of a third nitrogen-rich gas streams to said first adsorption zone; and

(j) countercurrently repressurizing the first adsorption zone by passing at least a portion of a fourth nitrogen-rich stream to said first adsorption zone.

3. The process of claim 2 wherein said process comprises a system of at least five adsorption zones and steps (a) through (j) are repeated in sequence for each adsorption zone.

4. The process of claim 2 wherein said process comprises a system of six adsorption zones and steps (a) through (j) are repeated in sequence for each adsorption zone.

5. The process of claim 2 wherein the feedstream additionally comprises at least one component selected from the group consisting of C₃ +hydrocarbons, C₂, CO₂, and mixtures thereof.

6. The process of claim 2 wherein the feedstream comprises from about 40 to 97 mol. % methane, from about 3 to 60 mol. % N₂, from about 0.1 to 10 mol. % ethane, from about 0.1 to 20 mol. % C₃ +hydrocarbons, and from about 0.1 to 20 mol. % CO₂.

7. The process of claim 2 wherein said adsorbent comprises activated carbon or mixtures of activated carbon and silica gel or activated alumina.

8. The process of claim 2 wherein the first pressure is from about 100 to 200 psia.

9. The process of claim 2 wherein the desorption pressure is from about 14.7 to 25 psia.

10. The process of claim 2 wherein the portion of product gas used to displace the nitrogen in step (b) ranges from 0.1 to 50 volume percent.

11. A pressure swing adsorption process comprising five-adsorption zones for the reduction of the nitrogen content of a gas feedstream comprising methane and nitrogen said process comprising:

(a) passing said feedstream cocurrently to a first adsorption zone containing an adsorbent material and void spaces to selectively adsorb methane and pressure the adsorption zone to a first pressure;

(b) discontinuing the passing of the feedstream to the first adsorption zone and cocurrently passing at least a portion of a first product gas stream to the first adsorption zone at a pressure sufficient to displace at least a portion of nitrogen from the void spaces and simultaneously venting a first nitrogen-rich stream from the process, thereby raising the pressure of said first adsorption zone to a second pressure;

(c) discontinuing the passing of said first product gas stream to said first adsorption zone and partially depressurizing the first adsorption zone to a third pressure by cocurrently withdrawing a second nitrogen-rich stream from said first adsorption zone and passing said second nitrogen-rich stream to a third adsorption zone to equalize pressure with said third adsorption zone;

(d) depressurizing the first adsorption zone to a fourth pressure by cocurrently withdrawing a third nitrogen-rich stream and passing said third nitrogen-rich stream to a fourth adsorption zone;

(e) depressurizing the first adsorption zone to a fifth pressure by cocurrently withdrawing a fourth nitrogen-rich gas stream to the fourth adsorption zone to equalize the pressure with said fourth adsorption zone;

(f) depressurizing the first adsorption zone to a sixth pressure by cocurrently withdrawing a fifth nitrogen-rich gas stream and passing said fifth nitrogen-rich stream to a fifth adsorption zone;

(g) cocurrently recovering a high heat content fuel gas stream from the first adsorption zone and reducing the pressure of the first adsorption zone to a seventh pressure;

(h) depressurizing the first adsorption zone to an eighth pressure by countercurrently recovering a second product gas stream;

(i) countercurrently purging the first adsorption zone with a sixth nitrogen-rich gas stream from a second adsorption zone and a seventh nitrogen-rich gas stream from the third adsorption zone and recovering a third product gas stream from the process;

(j) countercurrently repressurizing the first adsorption zone with an eighth nitrogen-rich gas stream from the third adsorption zone to a pressure greater than said sixth pressure;

(k) countercurrently repressurizing the first adsorption zone with a ninth nitrogen-rich gas stream from the fourth adsorption zone to a pressure greater than said fifth pressure; and

(l) repeating steps (a) through (k) in sequence for each of the five-adsorption zones.

12. The process of claim 11 wherein the feedstream additionally comprises at least one component selected from the group consisting of C₃ +hydrocarbons, C₂, CO₂, and mixtures thereof.

13. The process of claim 11 wherein the feedstream comprises from about 40 to 97 mol. % methane, from about 3 to 60 mol. % N₂, from about 0.1 to 10 mol. % ethane, from about 0.1 to 20 mol. % C₃ +hydrocarbons, and from about 0.1 to 20 mol. % CO₂.

14. The process of claim 11 wherein the adsorbent material comprises activated carbon and mixtures thereof with silica gel and/or activated alumina.

15. The process of claim 11 wherein the first pressure is from about 100 to 200 psia.

16. The process of claim 11 wherein the eighth pressure is from about 14.7 to 25 psia.

17. The process of claim 11 wherein the portion of product gas used to displace the nitrogen in step (b) ranges from 0.1 to 50 volume percent.

18. A pressure swing adsorption process comprising six-adsorption zones for the reduction of the nitrogen content of a gas feedstream comprising methane and nitrogen said process comprising:

(a) passing said feedstream cocurrently to a first adsorption zone containing an adsorbent material and void spaces to selectively adsorb methane and pressure the adsorption zone to a first pressure;

(b) discontinuing the passing of the feedstream to the first adsorption zone and cocurrently passing at least a portion of a first product gas stream to the first adsorption zone at a pressure sufficient to displace at least a portion of nitrogen from the void spaces and simultaneously venting a first nitrogen-rich stream from the process, thereby raising the pressure of said first adsorption zone to a second pressure;

(c) discontinuing the passing of said first product gas stream to said first adsorption zone and partially depressurizing the first adsorption zone to a third pressure by cocurrently withdrawing a second nitrogen-rich stream from said first adsorption zone and passing said second nitrogen-rich stream to a third adsorption zone to partially equalize pressure with said third adsorption zone;

(d) depressurizing the first adsorption zone to a fourth pressure by cocurrently withdrawing at least a portion of a third nitrogen-rich stream and passing said portion to a fifth adsorption zone, and passing the remaining portion of said third nitrogen-rich stream to a fourth adsorption zone to partially equalize the pressure with said fourth adsorption zone;

(e) depressurzing the first adsorption zone to a fifth pressure by cocurrently withdrawing a fourth nitrogen-rich stream and passing said fourth nitrogen-rich stream to a fifth adsorption zone to partially equalize the pressure with said fifth adsorption zone;

(f) cocurrently recovering a high heat content fuel gas stream from the first adsorption zone and reducing the pressure of the first adsorption zone to a sixth pressure;

(g) countercurrently depressurizing the first adsorption zone to a seventh pressure and recovering at least a portion of a second product gas stream from the process and passing a portion of said second product gas stream to a surge tank;

(h) countercurrently purging the first adsorption zone with a fifth nitrogen-rich gas stream from the third adsorption zone and recovering a third product gas stream from the process;

(i) countercurrently repressurizing the first adsorption zone with a sixth nitrogen-rich gas stream from the third adsorption zone to a pressure greater than said sixth pressure;

(j) countercurrently repressurizing the first adsorption zone with a seventh nitrogen-rich gas stream from the fourth adsorption zone to a pressure greater than said fourth pressure;

(k) countercurrently repressurizing the first adsorption zone with an eighth nitrogen-rich stream from the fifth adsorption zone to an eighth pressure; and

(1) repeating steps (a) through (k) in sequence for each of the six-adsorption zones.

19. The process of claim 18 wherein the feedstream additionally comprises at least one component selected from the group consisting of C₃ +hydrocarbons, C₂, CO₂, and mixtures thereof.

20. The process of claim 18 wherein the feedstream comprises from about 40 to 97 mol. % methane, from about 3 to 60 mol. % N₂, from about 0.1 to 10 mol. % ethane, from about 0.1 to 20 mol. % C₃ +hydrocarbons, and from about 0.1 to 20 mol. % CO₂.

21. The process of claim 18 wherein the adsorbent material comprises activated carbon and mixtures thereof with silica gel and/or activated alumina.

22. The process of claim 18 wherein the first pressure is from about 100 to 200 psia.

23. The process of claim 18 wherein the seventh pressure is from about 14.7 to 25 psia.

24. The process of claim 18 wherein the portion of product gas used to displace the nitrogen in step (b) ranges from 0.1 to 50 volume percent.