IP Library Granted Patent US 10,112,146
Granted Patent B2
US 10,112,146 · App. 14/809,769 · Granted Oct 30, 2018

Carbon dioxide capture system

Inventors: Koshito Fujita (Yokohama, JP); Hideo Kitamura (Katsushika, JP); Masatoshi Hodotsuka (Saitama, JP)
Assignee: KABUSHIKI KAISHA TOSHIBA
B01D53/78B01D53/1475B01D53/62B01D2252/204B01D2258/0283Y02A50/2342Y02C10/04Y02C10/06
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Quick Facts
Patent No.
US 10,112,146
App. No.
14/809,769
Granted
Oct 30, 2018
Kind
B2
Abstract

A carbon dioxide capture system according to an embodiment includes an absorber, a stripper, and a heater. The absorber includes a first cleaning unit and a second cleaning unit. The first cleaning unit uses first cleaning liquid to clean combustion exhaust gas discharged from a carbon dioxide capturer and captures amine flowing together with the combustion exhaust gas. The second cleaning unit uses second cleaning liquid to clean the combustion exhaust gas discharged from the first cleaning unit and captures amine flowing together with the combustion exhaust gas. The heater heats the first cleaning liquid to a temperature higher than the temperature of an upper portion of the carbon dioxide capturer and of the second cleaning liquid.

Claims (28)

1. A carbon dioxide capture system comprising:

a carbon dioxide capturer configured to cause carbon dioxide contained in combustion exhaust gas to be absorbed in an absorbing liquid containing amine and to discharge the combustion exhaust gas as decarbonated combustion exhaust gas;

a first cleaning unit configured to capture the amine flowing together with the decarbonated combustion exhaust gas discharged from the carbon dioxide capturer into first cleaning liquid supplied at a first temperature higher than a temperature at an upper portion of the carbon dioxide capturer,

a second cleaning unit configured to capture the amine flowing together with the decarbonated combustion exhaust gas discharged from the first cleaning unit into second cleaning liquid supplied at a second temperature lower than the first temperature,

a heater configured to heat the first cleaning liquid to the first temperature and to discharge the first cleaning liquid to the first cleaning unit,

a stripper configured to cause the carbon dioxide to be released from the absorbing liquid supplied from the carbon dioxide capturer; and

a reboiler configured to heat the absorbing liquid within the stripper with a heating medium and to discharge the heating medium therefrom,

wherein the heater includes a heating medium supply line configured to supply the heating medium from the reboiler to the first cleaning unit, and to mix the heating medium with the first cleaning liquid.

2. The carbon dioxide capture system according to claim 1 , further comprising

a demister provided between the first cleaning unit and the second cleaning unit and configured to capture mist flowing together with the decarbonated combustion exhaust gas discharged from the first cleaning unit.

3. The carbon dioxide capture system according to claim 1 , further comprising

a demister provided above the second cleaning unit and configured to capture mist flowing together with the decarbonated combustion exhaust gas discharged from the second cleaning unit.

4. The carbon dioxide capture system according to claim 1 ,

wherein the first cleaning unit and the second cleaning unit are so configured that the decarbonated combustion exhaust gas discharged from the first cleaning unit is directly supplied to the second cleaning unit.

5. The carbon dioxide capture system according to claim 1 ,

wherein the first cleaning unit is covered with a heat insulating material.

6. The carbon dioxide capture system according to claim 1 , further comprising

a cleaning liquid cooler configured to cool the second cleaning liquid.

7. The carbon dioxide capture system according to claim 6 ,

wherein the second cleaning unit is covered with a heat insulating material.

8. The carbon dioxide capture system according to claim 1 ,

wherein the second cleaning unit comprises:

an amine capturer configured to capture the amine flowing together with the decarbonated combustion exhaust gas; and

a cleaning liquid storage part provided below the amine capturer and configured to store the second cleaning liquid flowing downward from the amine capturer.

9. The carbon dioxide capture system according to claim 8 , further comprising

a bypass line configured to supply the second cleaning liquid from the cleaning liquid storage part of the second cleaning unit to the first cleaning unit.

10. The carbon dioxide capture system according to claim 1 , further comprising

a third cleaning unit configured to capture the amine flowing together with the decarbonated combustion exhaust gas discharged from the second cleaning unit into third cleaning liquid containing an acid.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 17, 2016
From: FUJITA, KOSHITO; KITAMURA, HIDEO; HODOTSUKA, MASATOSHI
To: KABUSHIKI KAISHA TOSHIBA
Reel/Frame 038011/0366 →
Priority Claims (1)
JP 2014-243518 · Dec 1, 2014 · national
Continuity (1)
Related Publication 20160151742A1 · Jun 2, 2016