A CO 2 recovery unit for recovery and removal of CO 2 in a CO 2 -containing flue gas using a CO 2 -absorbent within a CO 2 absorber is provided. The CO 2 absorber includes a CO 2 -absorbing unit for the absorption of CO 2 in a CO 2 -containing flue gas, a main water rinsing unit that is provided on a gas flow downstream side of the CO 2 -absorbing unit and that uses rinsing water to recover the accompanying CO 2 -absorbent while cooling decarbonated flue gas, and a preliminary water rinsing unit provided between the CO 2 -absorbing unit and the main water rinsing unit. A portion of the rinsing water containing the CO 2 -absorbent that is circulated in the main water rinsing unit is withdrawn and is subjected to preliminary water rinsing in the preliminary water rinsing unit. The preliminary rinsing water is allowed to meet with a CO 2 -absorbent while allowing the rinsing water to directly flow down on the CO 2 -absorbing unit side.
1. A CO 2 recovery unit comprising:
a CO 2 absorber configured to bring a CO 2 -containing flue gas containing CO 2 into contact with a CO 2 absorbent to remove CO 2 ; and
a CO 2 -absorbent regenerator configured to separate CO 2 from the CO 2 absorbent that has absorbed CO 2 therein, to regenerate the CO 2 absorbent and to separate condensed water from CO 2 gas accompanied by steam released therefrom;
a lean solution obtained by removing CO 2 in the absorbent regenerator being reutilized in the CO 2 absorber, and the condensed water being used in the CO 2 absorber,
the CO 2 absorber comprising:
a CO 2 -absorbing unit that absorbs CO 2 in a CO 2 -containing flue gas with the CO 2 absorbent;
a preliminary water rinsing unit that is provided on a gas flow downstream side of the CO 2 -absorbing unit and that preliminarily rinses decarbonated flue gas flowing from the CO 2 -absorbing unit;
a main water rinsing unit that is provided on the gas flow downstream side of the preliminary water rinsing unit and that rinses decarbonated flue gas flowing from the preliminary water rinsing unit;
a circulation line that is configured to circulate rinsing water in the main water rinsing unit;
a withdrawal line that is branched from the circulation line to withdraw a portion of the rinsing water circulating in the main water rinsing unit;
a cooling unit that is provided on the withdrawal line and is configured to cool the portion of the withdrawn rinsing water; and
a finish water rinsing unit that is provided on a rear stage side of the gas flow in the main water rinsing unit and is configured to finish rinse the decarbonated flue gas with the condensed water, wherein
the main water rinsing unit is configured to rinse the decarbonated flue gas while cooling with the rinsing water circulating in the main water rinsing unit via the circulating line to recover the CO 2 absorbent by which the decarbonated flue gas is accompanied; and
the preliminary water rinsing unit is configured to preliminarily rinse the decarbonated flue gas with the rinsing water withdrawn via the withdrawal line to recover the CO 2 absorbent by which the decarbonated flue gas is accompanied, and allow the preliminary rinsing water obtained by the preliminary water rinsing to directly flow down through the CO 2 -absorbing unit toward a lower side thereof, meet with the CO 2 absorbent through the CO 2 -absorbing unit, and come into countercurrent contact with the flue gas.
2. The CO 2 recovery unit according to claim 1 , further comprising a concentration unit that removes a volatile substance contained in a portion of the rinsing water withdrawn from the main water rinsing unit,
wherein concentrated water from which the volatile substance has been removed is supplied, as rinsing water, into the preliminary water rinsing unit.
3. The CO 2 recovery unit according to claim 1 , wherein the main water rinsing unit is provided in a plurality of stages.
4. A method for recovering CO 2 , using a CO 2 absorber configured to bring a CO 2 -containing flue gas into contact with a CO 2 absorbent to remove CO 2 , and a CO 2 -absorbent regenerator configured to separate CO 2 from the CO 2 absorbent that has absorbed CO 2 , to regenerate the CO 2 absorbent and to separate condensed water from CO 2 gas accompanied by steam released therefrom, a lean solution obtained by removing CO 2 in the absorbent regenerator being reutilized in the CO 2 absorber, and the condensed water being used in the CO 2 absorber, the method comprising:
rinsing decarbonated flue gas in a main rinsing unit while cooling with circulating rinsing water to recover the CO 2 absorbent by which the decarbonated flue gas is accompanied;
finish rinsing the decarbonated flue gas with the condensed water;
withdrawing a portion of the circulating rinsing water;
cooling the portion of the circulating rinsing water; and
preliminarily rinsing decarbonated flue gas prior to the rinsing in the main rinsing unit with the rinsing water withdrawn to recover the CO 2 absorbent by which the decarbonated flue gas is accompanied, and allowing the preliminary rinsing water obtained by the preliminary rinsing to directly flow down through a CO 2 -absorbing unit toward a lower side thereof, meet with the CO 2 absorbent through the CO 2 -absorbing unit, and come into countercurrent contact with the flue gas.
5. The method for recovering CO 2 according to claim 4 , wherein
concentrating the rinsing water withdrawn by removing a volatile substance therein to give concentrated water, and
using the concentrated water as rinsing water for preliminary rinsing.