CO2 rejection from natural gas

• US 20030047071A1
• Filed: 09/04/2001
• Published: 03/13/2003
• Est. Priority Date: 09/04/2001
• Status: Abandoned Application

• Current Assignee: Engelhard Corporation (BASF SE)
• Original Assignee: Engelhard Corporation (BASF SE)
• Inventors: Dolan, William B., Mitariten, Michael J.
• Application Number:
  US09/945,870
• Publication Number:
  US 20030047071A1
• Time in Patent Office: Days
• US Class Current: 95/96
• CPC Class Codes: B01D 2253/106 Silica or silicates
• CPC Class Codes: B01D 2253/311 Porosity, e.g. pore volume
• CPC Class Codes: B01D 2257/504 Carbon dioxide
• CPC Class Codes: B01D 2258/06 Polluted air
• CPC Class Codes: B01D 2259/40052 Recycled product or process gas
• CPC Class Codes: B01D 53/047 Pressure swing adsorption
• CPC Class Codes: C07C 7/12 by adsorption, i.e. purification or separation of hydrocarbons with the aid of solids, e.g. with ion-exchangers
• CPC Class Codes: C07C 9/04 Methane production by treatment of sewage C02F11/04; natural gas, synthetic natural gas C10L3/06
• CPC Class Codes: C10L 3/10 Working-up natural gas or synthetic natural gas
• CPC Class Codes: C10L 3/102 of acid contaminants
• CPC Class Codes: Y02C 20/40 of CO2
• CPC Class Codes: Y02P 20/151 Reduction of greenhouse gas [GHG] emissions, e.g. CO2

Abstract

An improved pressure swing adsorption process is provided for removing or separating a gas from a mixture of gases. The PSA process comprises selectively adsorbing a gas from the mixture to form a product gas having a reduced concentration of the selectively adsorbed gas and a low pressure purge stream containing a higher level of the selectively adsorbed gas than contained in the mixture. During regeneration of the adsorbent a co-current recycle stream is provided which has a pressure less than the product stream, but greater than the purge stream for recycle to feed so as to minimize loss of the product gas to purge. The PSA process is particularly useful for removing carbon dioxide from coal bed methane.

Claims

1. A pressure swing adsorption (PSA) process for the separation of a single gas from a mixture of gases which comprises:

a) passing a feed stream comprising said mixture in contact with an adsorbent which is selective for said single gas in a PSA unit so as to preferentially adsorb said single gas and produce a product depleted in said single gas and a low pressure purge stream having a higher concentration of said single gas than said mixture;

b) co-currently depressurizing said PSA unit to form a recycle stream having a lower concentration of said single gas than said purge stream, said recycle stream having a pressure less than said product stream, but greater than said purge stream; and

c) recycling said recycle stream to said feed stream.

2. The process of claim 1, wherein said purge stream is at a pressure of less than 10 psia and said recycle stream is at a pressure of 10 to 100 psia.

3. The process of claim 2, wherein said recycle stream is at a pressure of from 15 to 50 psia.

4. The process of claim 1, wherein said single gas is carbon dioxide.

5. The process of claim 4, wherein said mixture includes methane.

6. The process of claim 1, wherein said mixture of gases includes methane.

7. The method of claim 6, wherein said mixture comprises natural gas.

8. The process of claim 6, wherein said mixture comprises coal bed methane.

9. The process of claim 4, wherein said mixture comprises coal bed methane.

10. The process of claim 9, wherein said product stream comprises no more than 2 mol. % carbon dioxide.

11. The process of claim 7, wherein said single gas is carbon dioxide.

12. A pressure swing adsorption (PSA) process for the separation of carbon dioxide from a mixture of the same with methane which comprises:

a) passing a feed stream comprising said mixture in contact with a carbon dioxide-selective adsorbent in a PSA unit so as to preferentially adsorb carbon dioxide and produce a methane-rich product stream and a low pressure purge stream having a higher molar concentration of carbon dioxide than said mixture;

b) co-currently depressurizing said PSA unit to form a recycle stream rich in methane, said recycle stream having a pressure less than said methane-rich product stream, but greater than said purge stream; and

c) recycling said recycle stream to said feed stream.

13. The process of claim 12, wherein said mixture comprises natural gas.

14. The process of claim 12, wherein said mixture comprises coal bed methane.

15. The process of claim 12, wherein said mixture is at a pressure of 60 to 100 psia when in contact with said carbon dioxide selective adsorbent.

16. The process of claim 12, wherein said purge stream is at a pressure of less than 10 psia.

17. The process of claim 16, wherein said recycle stream is at a pressure of from 10 to 100 psia.

18. The process of claim 17, wherein said recycle stream is at a pressure of 15 to 50 psia.

19. The process of claim 12, wherein said methane-rich product stream contains no more than 2 mol. % carbon dioxide.

20. The process of claim 12, wherein said carbon dioxide selective adsorbent is silica gel.

21. The process of claim 20, wherein said silica adsorbent has a percentage of micropore volume of at least 15% relative to intrusion pore volume of said adsorbent as measured by the AutoPore IV 9500 and TriStar 3000, manufactured by Micrometrics, Norcross, Ga.

22. The process of claim 21, wherein said mixture comprises coal bed methane.