[Problem to be solved] A CO 2 recovery apparatus which can significantly reduce the amount of steam and provide further improved energy efficiency is provided. [Solution] The apparatus includes: a flue gas cooling apparatus 14 for allowing cooling water 13 to cool a CO 2 and O 2 containing flue gas 12 that is emitted from an industrial combustion facility 11 such as a boiler or gas turbine; a CO 2 absorber 16 having a CO 2 recovery section 16 A for bringing the cooled CO 2 containing flue gas 12 and a CO 2 absorbing CO 2 absorbent 15 into contact with each other to remove CO 2 from the flue gas 12 ; and an absorbent regenerator 18 for releasing CO 2 from a CO 2 absorbed CO 2 absorbent 17 to regenerate the CO 2 absorbent. The apparatus further includes: a cleansing water divert line 51 for diverting partial cleansing water 19 a of circulating cleansing water 19 that has been condensed in a cleansing section 16 B in the CO 2 absorber 16 ; a first heat exchanger 52 disposed in the divert line 51 and in a boiler flue gas duct 11 a ; and a superheated cleansing solution supply line 53 for directing, into the bottom portion of the absorbent regenerator 18 , a superheated cleansing solution 19 b having heat exchanged with a first heat exchanger 52.
1. A CO 2 recovery apparatus comprising:
a CO 2 absorber for bringing a CO 2 containing gas and a CO 2 absorbent into contact with each other so as to reduce CO 2 and release CO 2 reduced gas;
an absorbent regenerator for allowing a CO 2 absorbed rich solution to be regenerated in a regenerative superheater and outputting a CO 2 accompanying gas that accompanies water vapor; wherein a lean solution with CO 2 reduced in the absorbent regenerator is recycled in the CO 2 absorber as the CO 2 absorbent;
a cleansing section disposed downstream of a gas flow in the CO 2 absorber, for bringing the CO 2 reduced gas and a cleansing solution into contact with each other;
a reflux line for condensing the water vapor accompanied by the CO 2 accompanying gas so as to return the condensed water as reflux water to the absorbent regenerator;
a supplying line for adding a part of the reflux water to the cleansing solution;
a first heat exchanger disposed in a boiler flue gas duct, for extracting a part of the cleansing solution so as to exchange heat with the part of the cleansing solution; and
a superheated cleansing solution supply line for introducing the superheated cleansing solution that has heat exchanged in the heat exchange section into a bottom portion of the absorbent regenerator.
2. The CO 2 recovery apparatus according to claim 1 , wherein
the absorbent regenerator is divided at least into two, and
the CO 2 recovery apparatus comprises:
a semi-lean solution divert line for diverting a semi-lean solution with CO 2 partially reduced from an upper stage of the divided absorbent regenerator to supply to a lower stage of the absorbent regenerator, and
a steam condensed water heat exchanger, disposed in the semi-lean solution divert line, for heating the semi-lean solution by afterheat of steam condensed water from the regenerative superheater.
3. The CO 2 recovery apparatus according to claim 2 , wherein
the semi-lean solution divert line is provided with a lean solution heat exchanger for heating a semi-lean solution using heat of the lean solution from the absorbent regenerator.
4. The CO 2 recovery apparatus according to claim 1 , wherein
a rich/lean solution heat exchanger for heating the rich solution using afterheat of the lean solution is disposed at an intersection of a rich solution supply line for supplying the rich solution from the CO 2 absorber to the regenerative superheater and a lean solution supply line for supplying the lean solution from the absorbent regenerator to the CO 2 absorber.