Hybrid process using a membrane to enrich flue gas CO2 with a solvent-based post-combustion CO2 capture system

Patent metadata

Field	Value
Publication number	US-9409120-B2
Application number	US-201514591392-A
Country	US
Kind code	B2
Filing date	Jan 7, 2015
Priority date	Jan 7, 2014
Publication date	Aug 9, 2016
Grant date	Aug 9, 2016

Abstract

A process for recovery of CO 2 from a post-combustion gas includes pre-concentrating a CO 2 component of the post-combustion flue gas by passing the post-combustion gas through a CO 2 -selective membrane module to provide a CO 2 -enriched permeate stream and a CO 2 -lean reject stream. Next, in a CO 2 absorber, both the CO 2 -enriched permeate stream and CO 2 lean reject stream, fed to separate feed locations on the CO 2 absorber, are contacted with a scrubbing solvent to absorb CO 2 and provide a carbon-rich scrubbing solvent. Finally, absorbed CO 2 is stripped from the carbon-rich scrubbing solvent by a two-stage CO 2 stripping system. The CO 2 -selective membrane may be a high flux, low pressure drop, low CO 2 selectivity membrane. The two stage stripping system includes a primary CO 2 stripping column for stripping CO 2 from the carbon-rich scrubbing solvent exiting the CO 2 absorber, and a secondary CO 2 stripping column for stripping CO 2 from a carbon-lean scrubbing solvent exiting the primary CO 2 stripping column. Apparatus for CO 2 removal from post-combustion gases in a pulverized coal power plant incorporating the described processes are described.

First claim

What is claimed:

1. A process for removal and recovery of CO 2 from a post-combustion flue gas, comprising:
pre-concentrating a CO 2 component of the post-combustion flue gas by passing the post-combustion flue gas through a CO 2 -selective membrane module to provide a CO 2 -enriched permeate stream and a CO 2 -lean reject stream;
in a CO 2 absorber, contacting the CO 2 -enriched permeate stream and the CO 2 -lean reject stream with a scrubbing solvent to absorb CO 2 and provide a carbon-rich scrubbing solvent; and
stripping absorbed CO 2 from the carbon-rich scrubbing solvent by a two-stage CO 2 stripping system.

2. The process of claim 1 , further including evaporating at least a portion of a water component of a post-combustion flue gas condensate for use as a carrier vapor for a permeate side of the CO 2 -selective membrane module.

3. The process of claim 1 , further including passing a CO 2 -rich permeate stream from the CO 2 -selective membrane module to a feed point disposed at a bottom portion of the CO 2 absorber and passing the CO 2 -lean reject stream from the CO 2 -selective membrane module to an intermediate feed point above the CO 2 absorber bottom portion feed point.

4. The process of claim 1 , further including providing a CO 2 -membrane module comprising a high flux, low pressure drop, low CO 2 selectivity membrane.

5. The process of claim 1 , further including providing a two stage stripping system comprising:
a primary CO 2 stripping column for stripping CO 2 from the carbon-rich scrubbing solvent exiting the CO 2 absorber; and
a secondary CO 2 stripping column for stripping CO 2 from a carbon-lean scrubbing solvent exiting the primary CO 2 stripping column.

6. The process of claim 5 , including providing an ambient pressure air-swept, packed column secondary CO 2 stripping column.

7. The process of claim 1 , including providing a CO 2 absorber having a bottom packing portion with a first cross-sectional dimension, and a top packing portion with a second cross-sectional dimension that is different from the first cross-sectional dimension.

8. The process of claim 1 , including providing one or more intercoolers at intermediate positions of the CO 2 absorber.

9. The process of claim 7 , wherein the first cross-sectional dimension is approximately ⅓ that of the second cross-sectional dimension.

10. The process of claim 6 , including passing a CO 2 -enriched air source exiting the secondary CO 2 stripping column to a preheater and therefrom as a boiler combustion air for a pulverized coal boiler of a pulverized coal plant.

11. A CO 2 capture and recovery system for recovery of CO 2 from a post-combustion gas, comprising:
a CO 2 -selective membrane module for pre-concentrating a CO 2 component of an SO 2 -depleted post-combustion gas to provide a CO 2 -enriched permeate stream and a CO 2 -lean reject stream;
a CO 2 absorber for providing a carbon-rich scrubbing solvent by contacting the CO 2 -enriched permeate stream and the CO 2 -lean reject stream with a scrubbing solvent to absorb CO 2 ; and
a two-stage CO 2 stripping system for stripping absorbed CO 2 from the carbon-rich scrubbing solvent.

12. The system of claim 11 , further including a moisture separator or condenser for removing at least a portion of a water vapor component of the CO 2 -enriched permeate stream.

13. The system of claim 11 , wherein the CO 2 -enriched permeate stream from the CO 2 -selective membrane module is passed to a feed point disposed at a bottom of the CO 2 absorber and the CO 2 -lean reject stream from the CO 2 -selective membrane module is passed to an intermediate feed point above the CO 2 -absorber bottom feed point.

14. The system of claim 11 , wherein the CO 2 -membrane module comprises a high flux, low pressure drop, low CO 2 -selectivity membrane.

15. The system of claim 11 , wherein the two stage stripping system comprises:
a primary CO 2 stripping column for stripping CO 2 from the carbon-rich scrubbing solvent exiting the CO 2 absorber; and
a secondary CO 2 stripping column for stripping CO 2 from a carbon-lean scrubbing solvent exiting the primary CO 2 stripping column.

16. The system of claim 15 , wherein the secondary CO 2 stripping column is an ambient pressure air-swept, packed column CO 2 stripping column.

17. The system of claim 15 , wherein the CO 2 absorber includes a bottom packing portion with a first cross-sectional dimension and a top packing portion with a second cross-sectional dimension that is different from the first cross-sectional dimension.

18. The system of claim 11 , wherein the CO 2 absorber further includes one or more intercoolers disposed at intermediate positions of the CO 2 absorber.

19. The system of claim 17 , wherein the first cross-sectional dimension is approximately ⅓ that of the second cross-sectional dimension.

20. The system of claim 16 , wherein a CO 2 -enriched air source exiting the secondary CO 2 stripping column is passed to a preheater and therefrom to a pulverized coal boiler of a pulverized coal power plant as a boiler combustion air.

21. A pulverized coal-fired power plant comprising the CO 2 capture and recovery system of claim 11 .

Assignees

• Univ Kentucky Res Found
• The Univ Of Kentucky Res Found

Inventors

• Liu Kunlei
• Frimpong Reynolds A
• Liu Kun

Classifications

• B01D2053/221

  Devices · CPC title

• Y02E20/18

  Integrated gasification combined cycle [IGCC], e.g. combined with carbon capture and storage [CCS] · CPC title

• Y02C10/10

  Cross-Sectional Technologies · mapped topic

• B01D53/1443

  Pretreatment by diffusion · CPC title

• F01K23/067

  the combustion heat coming from a gasification or pyrolysis process, e.g. coal gasification (gas turbines with fuel gasifiers F02C3/28) · CPC title