IP Library Granted Patent US 10,201,778
Granted Patent B2
US 10,201,778 · App. 15/470,804 · Granted Feb 12, 2019

Process for separating CO2 from CO2 containing gas stream

Inventors: Youzong Gu (Beijing, CN); Wenqiang Xu (Beijing, CN)
Assignees: China Energy Investment Corporation Limited; National Institute of Clean-and-Low-Carbon Energy
B01D53/1475B01D53/1425B01D53/1493B01D53/62B01D2252/00B01D2257/504
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Quick Facts
Patent No.
US 10,201,778
App. No.
15/470,804
Granted
Feb 12, 2019
Kind
B2
Abstract

The invention relates to gas separation, particularly to a process for separating CO 2 from a CO 2 containing gas stream with varying CO 2 concentration using a membrane-based separation system. The process for separating CO 2 comprises: (i) feeding the CO 2 containing gas stream into a membrane-based separation system comprising one or more membrane stages in-line, each membrane stage producing a CO 2 -depleted retentate stream and a rich CO 2 permeate stream, and (ii) recycling a part of the CO 2 -rich permeate stream from at least one membrane stage as a recycled stream, into a preceding feed stream of one or more membrane stages in the membrane-based separation system to adjust the CO 2 concentration of the feed stream. The process could stabilize the CO 2 concentration in the feed steam by recirculation of a fraction of the high purity CO 2 permeate to the feed of the membrane system, which would result in a lower incremental auxiliary load than other options such as compression of the entire gas stream.

Claims (18)

1. A process for separating CO 2 from a CO 2 containing gas stream with varying CO 2 concentration in time comprising:

(i) feeding the CO 2 containing gas stream with varying CO 2 concentration into a membrane-based separation system comprising one or more membrane stages in-line, each membrane stage producing a CO 2 -depleted retentate stream and a CO 2 -rich permeate stream, and

(ii) recycling a part of the CO 2 -rich permeate stream of one or more membrane stages as a recycled stream, into a preceding feed stream of one or more membrane stages in the membrane-based separation system to adjust the CO 2 concentration of the feed stream to keep the CO 2 concentration in the feed stream to one or more of stages of the membrane-based separation system steady, the flow rate of the recycled stream is adjusted based on measurements of the CO 2 concentration of the feed stream, or the flow rate of the recycled stream is adjusted based on upstream parameters in accordance with which the CO 2 containing gas stream is generated including: operational parameters of the plant where the CO 2 containing gas stream is generated, or operational parameters related to upstream emissions controls of the CO 2 containing gas stream.

2. The process according to claim 1 wherein the CO 2 containing gas stream is a flue gas stream produced from power generation using fossil fuels.

3. The process according to claim 2 , wherein the fossil fuel is coal.

4. The process according to claim 1 further comprising using a part of the last CO 2 -rich permeate stream from the last membrane stage as the recycled stream.

5. The process according to claim 1 further comprising recycling at least a part of the recycled stream into the first feed stream of the first membrane stage.

6. The process according to claim 5 wherein the CO 2 concentration of the first feed stream is adjusted to 12 mol % or more by the recycled stream.

7. The process according to claim 6 wherein the CO 2 concentration of the first feed stream is adjusted to 12 mol % - 15 mol % by the recycled stream.

8. The process according to claim 1 wherein the flow rate of the recycled stream is 70 mol % or less based on total content of the last CO 2 -rich permeate stream.

9. The process according to claim 8 wherein the flow rate of the recycled stream is 25 mol % - 70 mol % based on total content of the last CO 2 -rich permeate stream.

10. The process according to claim 9 wherein the flow rate of the recycled stream is 30 mol % - 65 mol % based on total content of the last CO 2 -rich permeate stream.

11. The process according to claim 1 wherein the recycled stream enables the total content of the feed stream to be increased by 15 mol % or less.

12. The process according to claim 1 wherein overall CO 2 recovery rate is 50% or more.

13. The process according to claim 12 wherein the overall CO 2 recovery rate is 60% - 90%.

14. The process according to claim 1 wherein the concentration of CO 2 in the last permeate stream is 60 mol % or above.

15. The process according to claim 14 wherein the concentration of CO 2 in the last permeate stream is 90 mol % or above.

16. The process according to claim 14 wherein the concentration of CO 2 in the last permeate stream is 95 mol % or above.

Assignments (2)
CHANGE OF NAME Recorded Jul 18, 2018
From: SHENHUA GROUP CORPORATION LIMITED
To: CHINA ENERGY INVESTMENT CORPORATION LIMITED
Reel/Frame 046583/0623 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 27, 2017
From: GU, YOUZONG; XU, WENQIANG
To: SHENHUA GROUP CORPORATION LIMITED; NATIONAL INSTITUTE OF CLEAN-AND-LOW-CARBON ENERGY
Reel/Frame 042102/0357 →
Priority Claims (1)
CN 2017 1 0058282 · Jan 23, 2017 · national
Continuity (1)
Related Publication 20180207577A1 · Jul 26, 2018
Cited By (1)
US 12,420,228