Process for separating selected components from multi-component natural gas streams

• US 5,660,603 A
• Filed: 09/05/1995
• Issued: 08/26/1997
• Est. Priority Date: 09/05/1995
• Status: Expired due to Fees

• Current Assignee: International Process Services, Inc. (Bechtel Group Incorporated)
• Original Assignee: International Process Services, Inc. (Bechtel Group Incorporated)
• Inventors: Chen, Jong J., Elliot, Douglas G.
• Primary Examiner(s): MCMAHON, TIMOTHY M
• Application Number:
  US08/523,719
• Time in Patent Office: 721 Days
• Field of Search: 48/127.3, 48/127.5, 48/190, 423/220, 585/15, 62/632, 62/633, 62/929
• US Class Current: 48/127.5
• CPC Class Codes: B01D 2257/504 Carbon dioxide
• CPC Class Codes: B01D 53/14 by absorption
• CPC Class Codes: B01D 53/1425 Regeneration of liquid absorbents
• CPC Class Codes: C01B 32/50 Carbon dioxide
• CPC Class Codes: C07C 7/00 Purification; Separation; Use of additives working-up undefined gaseous mixtures obtained by cracking hydrocarbon oils C10G70/00
• CPC Class Codes: C07C 9/04 Methane production by treatment of sewage C02F11/04; natural gas, synthetic natural gas C10L3/06
• CPC Class Codes: C07C 9/06 Ethane
• CPC Class Codes: Y02C 20/40 of CO2
• CPC Class Codes: Y02P 20/151 Reduction of greenhouse gas [GHG] emissions, e.g. CO2

Abstract

A process for separating components of gas mixtures which have different hydrate forming characteristics which uses an aqueous liquid to absorb one of the gases preferentially by attaining conditions slightly above the catastrophic point at which gas hydrates form. Specifically, the separation of gas mixtures containing light hydrocarbons and carbon dioxide is accomplished without significantly reducing the pressure of the carbon dioxide or without requiring significant amounts of heat energy for regeneration.

Claims

1. A method of separating a mixture of gases, one of which is a hydrocarbon gas comprising:

contacting the mixture of gases with an aqueous liquid; and

controlling the temperature and/or pressure during said contact such that the temperature of the liquid and gases during contact is slightly above the catastrophic temperature and within about 20°

C. above the catastrophic temperature to selectively retain one or more of the gases.

2. The process of claim 1, wherein said aqueous liquid is water.

3. The process of claim 1, wherein said aqueous liquid is a sodium chloride solution.

4. The process of claim 1, wherein said aqueous liquid is sea water.

5. The process of claims 1, wherein said aqueous solution is water containing a water soluble salt.

6. The process of claim 1, wherein said hydrocarbon gas is methane.

7. The process of claim 1, wherein said hydrocarbon gas is ethane.

8. The process of claim 1, wherein said mixture of gases includes natural gas.

9. The process of claim 1, including:

regenerating said aqueous liquid, to release the gases selectively retained in the aqueous liquid.

10. The process of claim 9, wherein said aqueous liquid regeneration comprises regulating either the temperature or pressure of said aqueous liquid away from the catastrophic point for hydrate formation.

11. A method for removing carbon dioxide from a hydrocarbon gas stream containing about 4 to about 90% carbon dioxide, the process comprising:

contacting said carbon dioxide containing hydrocarbon gas stream with an aqueous solution comprising a water soluble salt in water up to the solubility limits; and

controlling the pressure and/or the temperature such that the temperature of the aqueous solution and gas stream during the contacting is slightly above the catastrophic temperature and within about 20°

C. above the catastrophic temperature to selectively retain the carbon dioxide.

12. The process of claim 11, wherein said hydrocarbon gas is methane.

13. The process of claim 11, wherein said hydrocarbon gas is ethane.

14. A method of separating a mixture of gases, one of which is a hydrocarbon gas, comprising:

introducing an aqueous solution of water soluble salt and water into an absorption column;

introducing the mixture of gases into the absorption column;

controlling the temperature and pressure within said column such that the temperature is slightly above the catastrophic temperature and within about 20°

C. above the catastrophic temperature to selectively retain one gas from the mixture of gases without forming solid hydrate structures; and

separating the aqueous solution and the selectively retained gas from the gases not retained whereby a substantial separation of at least one gas from the mixture of gases occurs.

15. The process of claim 14, wherein the mixture of gases comprises carbon dioxide and methane and the carbon dioxide is selectively retained.

16. The process of claim 14, wherein the temperature and pressure within said column is controlled such that the temperature is within about 12°

C. above the catastrophic temperature.

17. The process of claim 14, wherein the temperature and pressure within said column is controlled such that the temperature is within about 6°

C. above the catastrophic temperature.