An absorption column is equipped with: a CO 2 absorption section absorbing CO 2 from CO 2 -containing exhaust gas using a lean solution; a main rinse section recovering an entrained CO 2 absorbent using rinse water; a rinse water circulation line circulating a rinse water containing the CO 2 absorbent recovered in a liquid storage section of the main rinse section; a pre-rinse section provided between the CO 2 absorption section and the main rinse section; a rinse section extraction liquid supply line extracting a portion of the rinse water containing the CO 2 absorbent from the rinse water circulation line, and introducing the same into a reflux section of an absorption liquid regeneration tower; and a refluxed water supply line extracting a portion of refluxed water, introducing the same as pre-rinse water for the pre-rinse section, and connected on the pre-rinse section side.
1. A CO 2 recovery device comprising:
a CO 2 absorption column that brings a CO 2 -containing flue gas containing CO 2 into contact with a CO 2 absorption liquid and removes CO 2 ; and
an absorption liquid regeneration column that regenerates the CO 2 absorption liquid that has absorbed the CO 2 ,
wherein a lean solution, from which CO 2 has been removed in the absorption liquid regeneration column, is reused in the CO 2 absorption column,
the CO 2 absorption column includes
a CO 2 absorption section that absorbs CO 2 in the CO 2 -containing flue gas with the CO 2 absorption liquid,
a main rinse section that is provided on a gas flow downstream side of the CO 2 absorption section, cools flue gas after CO 2 removal with rinse water, and recovers an entrained CO 2 absorbent with the rinse water,
a rinse water circulation line that supplies and circulates the rinse water containing the CO 2 absorbent recovered in a liquid storage section of the main rinse section from a top part side of the main rinse section,
a pre-rinse section that is provided between the CO 2 absorption section and the main rinse section,
a rinse section extraction liquid supply line that extracts a portion of the rinse water containing the CO 2 absorbent from the rinse water circulation line, is connected to a top part side of a reflux section, of the absorption liquid regeneration column, and introduces the portion of the rinse water into the reflux section, and
a refluxed water supply line that extracts a portion of refluxed water from a side closer to a column bottom part than an introduction position of the reflux section, is connected to the pre-rinse section side, and introduces the portion of the refluxed water as pre-rinse water of the pre-rinse section.
2. The CO 2 recovery device according to claim 1 , further comprising:
a deep rinse section that is provided on a gas flow downstream side of the main rinse section, and further performs deep rinsing of the flue gas after CO 2 removal after main rinsing with rinse water supplied from the outside.
3. The CO 2 recovery device according to claim 1 ,
wherein the pre-rinse section includes a pre-rinse water circulation line that supplies and circulates pre-rinse water from a top part side of the pre-rinse section, and
wherein the refluxed water supply line is connected to the pre-rinse water circulation line, and a portion of the refluxed water is introduced as the pre-rinse water.
4. The CO 2 recovery device according to claim 3 , further comprising:
a deep rinse section that is provided on a gas flow downstream side of the main rinse section, and further performs deep rinsing of the flue gas after CO 2 removal after main rinsing with rinse water supplied from the outside.
5. A CO 2 recovery method of reusing a lean solution, from which CO 2 has been removed in an absorption liquid regeneration column, in a CO 2 absorption column, using the CO 2 absorption column that brings a CO 2 -containing flue gas containing CO 2 into contact with a CO 2 absorption liquid and removes CO 2 , and an absorption liquid regeneration column that regenerates the CO 2 absorption liquid that separates CO 2 from the CO 2 absorption liquid that has absorbed the CO 2 , the method comprising:
pre-rinsing the CO 2 -removed flue gas using pre-rinse water extracted from a portion of reflux section obtained by a portion of rinse water used for the main rinsing being extracted, introduced into a reflux section of the absorption liquid regeneration column, and mixed with high-temperature refluxed water in the reflux section when main rinsing of CO 2 -removed flue gas is performed with rinse water on a downstream side of the CO 2 absorption column, and pre-rinsing of the CO 2 -removed flue gas after CO 2 recovery is performed on an upstream side where the main rinsing is performed.
6. The CO 2 recovery method according to claim 5 ,
wherein deep rinsing is performed with deep rinsing water supplied from the outside of a rinse section on a downstream side of the main rinse section.