CO2 recovery system and CO2 recovery method

Patent metadata

Field	Value
Publication number	US-9238191-B2
Application number	US-201313938760-A
Country	US
Kind code	B2
Filing date	Jul 10, 2013
Priority date	Dec 3, 2009
Publication date	Jan 19, 2016
Grant date	Jan 19, 2016

Abstract

A CO2 recovery system includes an absorber 2 and a regenerator 3 . The absorber 2 includes a CO2 absorbing section 21 and at least one water-washing section 22 . The CO2 absorbing section 21 allows flue gas 101 to come into contact with a basic amine compound absorbent 103 so that the basic amine compound absorbent 103 absorbs CO2 in the flue gas 101 . The at least one water-washing section 22 allows the decarbonated flue gas 101 A in which the amount of CO2 has been reduced in the CO2 absorbing section 21 to come into contact with wash water 104 A and 104 B to reduce the amounts of the basic amine compounds entrained in the decarbonated flue gas 101 A. The regenerator 3 releases the CO2 from the basic amine compound absorbent 103 containing CO2 absorbed therein.

First claim

The invention claimed is:

1. A CO 2 recovery method, comprising the steps of:
bringing flue gas into contact with a basic amine compound absorbent so that the basic amine compound absorbent absorbs CO 2 contained in the flue gas;
bringing the decarbonated flue gas in which an amount of CO 2 has been reduced into contact with wash water to reduce amounts of basic amine compounds entrained in the decarbonated flue gas;
releasing the CO 2 from the basic amine compound absorbent containing the CO 2 absorbed therein; and
bringing circulating acidic water into contact with the decarbonated flue gas that has undergone the step of bringing the decarbonated flue gas into contact with the wash water to thereby further reduce the amounts of the basic amine compounds entrained in the decarbonated flue gas,
wherein the step of releasing the CO 2 from the basic amine compound absorbent includes the step of adding basic sodium to the basic amine compound absorbent, and
wherein part of the acidic water containing the basic amine compounds removed from the decarbonated flue gas is supplied to the step of adding basic sodium.

2. The CO 2 recovery method of claim 1 , wherein the step of bringing the circulating acidic water into contact with the decarbonated flue gas includes the step of adjusting a pH value of the acidic water to a desired value for obtaining salts of the basic amine compounds by contact with the decarbonated flue gas.

3. The CO 2 recovery method of claim 1 , further comprising the step of concentrating the acidic water before the part of the acidic water containing the basic amine compounds removed from the decarbonated flue gas is supplied to the step of adding basic sodium.

4. The CO 2 recovery method of claim 1 , further comprising, after the step of bringing the acidic water into contact with the decarbonated flue gas, the step of rendering harmless the acidic water containing the basic amine compounds removed from the decarbonated flue gas.

5. The CO 2 recovery method of claim 4 , further comprising the step of concentrating the acidic water before the step of rendering harmless the acidic water containing the basic amine compounds.

6. The CO 2 recovery method of claim 1 , wherein the step of bringing the acidic water into contact with the decarbonated flue gas includes the step of collecting the acidic water in a mist form that is entrained in the decarbonated-deaminated flue gas in which the amounts of the basic amine compounds have been reduced.

7. The CO 2 recovery method of claim 1 , wherein the step of bringing the acidic water into contact with the decarbonated flue gas includes the step of supplying, as replenishing water for the acidic water, condensed water generated when CO 2 gas recovered from the basic amine compound absorbent is cooled or condensed water that is used to cool the flue gas before CO 2 is absorbed thereinto.

8. The CO 2 recovery method of claim 1 , further comprising the steps of:
measuring a concentration of the basic amine compounds in the decarbonated-deaminated flue gas in which the amounts of the basic amine compounds have been reduced; and
adjusting a pH value of the acidic water or a flow rate of the acidic water on the basis of the measured concentration of the basic amine compounds.

9. The CO 2 recovery method of claim 1 , further comprising the step of reducing amounts of volatile organic compounds entrained in the decarbonated flue gas together with the basic amine compounds by bringing the decarbonated flue gas into contact with the acidic water.

10. The CO 2 recovery method of claim 9 , further comprising the steps of:
measuring a concentration of the volatile organic compounds in the decarbonated-deaminated flue gas in which the amounts of the volatile organic compounds and the amounts of the basic amine compounds have been reduced; and
adjusting the flow rate of the acidic water supplied to the step of reducing the amounts of the volatile organic compounds on the basis of the measured concentration of the volatile organic compounds.

Assignees

• Nagayasu Hiromitsu
• Kamijo Takashi
• Yonekawa Takahito
• Tanaka Hiroshi
• Kishimoto Shinya
• Hirata Takuya
• Tsujiuchi Tatsuya
• Chiyomaru Masaru
• Nakayama Koji
• Tatsumi Masahiko
• Yagi Yasuyuki
• Kaibara Kazuhiko
• Mitsubishi Heavy Ind Ltd
• Kansai Electric Power Co

Inventors

• Nagayasu Hiromitsu
• Kamijo Takashi
• Yonekawa Takahito
• Tanaka Hiroshi
• Kishimoto Shinya
• Hirata Takuya
• Tsujiuchi Tatsuya
• Chiyomaru Masaru
• Nakayama Koji
• Tatsumi Masahiko
• Yagi Yasuyuki
• Kaibara Kazuhiko

Classifications

• Y02C20/40

  of CO2 · CPC title

• Y02A50/20

  Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters · CPC title

• B01D53/1418 Primary

  Recovery of products · CPC title

• Y02C10/06

  Cross-Sectional Technologies · mapped topic

• B01D2252/204

  Amines · CPC title