Membrane separation of carbon dioxide from natural gas with energy recovery

Patent metadata

Field	Value
Publication number	US-10060348-B2
Application number	US-201414496240-A
Country	US
Kind code	B2
Filing date	Sep 25, 2014
Priority date	Sep 25, 2014
Publication date	Aug 28, 2018
Grant date	Aug 28, 2018

Abstract

Carbon dioxide is separated from natural gas using a single stage membrane separation system to produce a retentate gas that typically meets the specification for pipeline distribution of natural gas, and a permeate gas comprising methane that is combusted to generate power and/or heat, e.g. for use in providing the utility requirements of the process itself or for export to an integrated process. Advantages include an overall reduction in power consumption and improvement in process efficiency.

First claim

The invention claimed is:

1. A process for separating carbon dioxide from natural gas, said process comprising:
providing a natural gas feed comprising carbon dioxide;
introducing the natural gas feed to a single stage membrane separation system for separation of carbon dioxide from said natural gas feed to produce methane-enriched retentate gas and carbon dioxide-enriched permeate gas comprising methane;
monitoring the flow rate and composition of the permeate gas to determine the heat content of the permeate gas;
combining an auxiliary stream with at least a portion of the permeate gas to form a feed stream for a combustion system, wherein the heat content of the feed stream for the combustion system is normalized by controlling the flow of the auxiliary stream based on the monitored flow rate and composition;
combusting the feed stream for the combustion system in the combustion system to generate a combustion exhaust gas; and
recovering energy from said combustion;
wherein the single stage membrane separation system comprises a plurality of polymeric membrane units in series, and wherein the retentate from one polymeric membrane unit of the plurality of polymeric membrane units is fed to an adjacent downstream polymeric membrane unit of the plurality of polymeric membrane units without recompression;
wherein the auxiliary stream comprises a bypass stream withdrawn from and comprising a portion of the natural gas feed to the single stage membrane separation system.

2. The process according to claim 1 , wherein said natural gas feed has a higher heating value of at least about 780 BTU/scf (31 MJ/Nm 3 ).

3. The process according to claim 1 , wherein said natural gas feed comprises at least about 1.5% carbon dioxide.

4. The process according to claim 1 , wherein said natural gas feed comprises no more than about 97% methane.

5. The process according to claim 1 , wherein said natural gas feed is introduced to said single stage membrane separation system at a pressure from about 275 psi (19 bar) to about 1200 psi (85 bar).

6. The process according to claim 1 , wherein said natural gas feed is introduced to said single stage membrane separation system at a temperature from about 40° C. to about 80° C.

7. The process according to claim 1 , wherein said permeate gas has a higher heating value of at least about 400 BTU/scf (15 MJ/Nm 3 ).

8. The process according to claim 1 , wherein said permeate gas is compressed prior to said combustion.

9. The process according to claim 1 , wherein energy is recovered as power from at least a portion of said combustion exhaust gas using at least one turbine generating a turbine exhaust gas.

10. The process according to claim 1 , wherein energy is recovered as heat from at least a portion of said combustion exhaust gas by indirect heat exchange with a heat transfer fluid.

11. The process according to claim 1 , wherein said feed stream for the combustion system is combusted together with a secondary fuel.

12. The process according to claim 1 , wherein energy is recovered as power, at least a portion of which is used to provide compression duty.

13. The process according to claim 1 , wherein energy is recovered as heat, at least a portion of which is used to provide utility heating duty.

14. The process according to claim 1 , wherein the plurality of polymeric membrane units in series comprise from two to four polymeric membrane units in series.

15. The process according to claim 1 , wherein the plurality of polymeric membrane units in series comprise at least one polymeric membrane unit in which the membrane(s) has a CO 2 /CH 4 selectivity of at least about 5.

16. The process according to claim 1 , wherein the plurality of polymeric membrane units in series comprise at least one polymeric membrane unit in which the membrane(s) have a CO 2 /CH 4 selectivity of no more than about 100.

17. The process according to claim 1 , wherein the plurality of polymeric membrane units in series comprise at least one polymeric membrane unit comprising polyimide membranes.

18. The process according to claim 1 , wherein overall methane recovery is no more than 95%.

Assignees

• Air Prod & Chem

Inventors

• Ploeger Jason Michael
• Palamara John Eugene
• Kindt Jack Theodore

Classifications

• F02C3/22 Primary

  the fuel or oxidant being gaseous at standard temperature and pressure (F02C3/28 takes precedence) · CPC title

• F02C9/28

  Regulating systems responsive to plant or ambient parameters, e.g. temperature, pressure, rotor speed (F02C9/30 - F02C9/38, F02C9/44 take precedence) · CPC title

• F02C9/40

  specially adapted to the use of a special fuel or a plurality of fuels · CPC title

• F23R3/36

  Supply of different fuels · CPC title

• B01D2053/221

  Devices · CPC title