A CO 2 recovery apparatus includes a desulfurization tower which includes a desulfurization unit and a cooling unit, an absorption tower which includes a CO 2 absorption unit and an acid washing unit, a regeneration tower, and an acid water production device configured to produce acid water by causing exhaust gas yet to be introduced into the desulfurization to come into contact with water. In the CO 2 recovery apparatus, the water to be come in contact with the exhaust gas is condensed water that is generated in the desulfurization tower, the absorption tower, or the regeneration tower.
1. A CO 2 recovery apparatus comprising:
a desulfurization tower which includes:
a desulfurization unit configured to remove a sulfur content contained in exhaust gas; and
a cooling unit configured to cool desulfurized exhaust gas, from which the sulfur content has been removed by the desulfurization unit, by using cooling water;
an absorption tower which includes:
a CO 2 absorption unit configured to absorb CO 2 contained in the desulfurized exhaust gas, from which the sulfur content has been removed by the desulfurization tower, into a basic amine compound absorbing solution by causing the desulfurized exhaust gas to come into contact with the basic amine compound absorbing solution;
a washing unit configured to wash decarbonated exhaust gas, from which CO 2 has been removed by the CO 2 absorption unit, by causing the decarbonated exhaust gas to come into contact with washing water; and
an acid washing unit configured to remove a basic amine compound entrained in the decarbonated exhaust gas, from which CO 2 has been absorbed by the CO 2 absorption unit, by causing the decarbonated exhaust gas to come into contact with acid water; and
a regeneration tower configured to emit CO 2 gas and configured to regenerate the absorbing solution with heating to separate CO 2 and subsequently remove CO 2 from the absorbing solution; and
an acid water production device configured to produce the acid water by causing the exhaust gas yet to be introduced into the desulfurization unit to come into contact with water,
wherein the water to come into contact with the exhaust gas is condensed water generated by the desulfurization tower, the absorption tower, or the regeneration tower.
2. The CO 2 recovery apparatus according to claim 1 , wherein the acid water production device is provided in the desulfurization tower.
3. The CO 2 recovery apparatus according to claim 1 , further comprising:
a water level sensor configured to measure a water level of the acid water in the acid water production device;
a pH sensor configured to measure a pH value of the acid water; and
a control unit configured to control the pH value and the water level of the acid water by controlling exhaust gas and the condensed water to be supplied to the acid water production device and water drained from the acid water production device according to measurement values measured by the water level sensor and the pH sensor.
4. The CO 2 recovery apparatus according to claim 1 , further comprising:
a pH sensor configured to measure a pH value of acid water circulating in the acid washing unit;
a flow sensor configured to measure a flow rate of the acid water to be supplied to the acid washing unit; and
a control unit configured to control the pH value and the flow rate of the acid water to come into contact with the decarbonated exhaust gas by adjusting the flow rate of the acid water to be supplied to the acid washing unit according to a measurement value measured by the pH sensor.
5. A CO 2 recovery method comprising:
desulfurizing exhaust gas by removing a sulfur content contained in exhaust gas;
cooling the exhaust gas;
absorbing CO 2 contained in desulfurized exhaust gas, from which the sulfur content has been removed by the desulfurizing, into a basic amine compound absorbing solution by causing the desulfurized exhaust gas to come into contact with the basic amine compound absorbing solution;
emitting CO 2 gas and regenerating the absorbing solution with heating to separate CO 2 and subsequently remove CO 2 from the absorbing solution;
washing the decarbonated exhaust gas, from which CO 2 has been removed by the absorbing of CO 2 , by causing the decarbonated exhaust gas to come into contact with washing water;
removing a basic amine compound entrained in the decarbonated exhaust gas, which has been washed by the washing, from the exhaust gas by causing the decarbonated exhaust gas to come into contact with acid water; and
producing the acid water by causing the exhaust gas yet to be subjected to the desulfurizing to come into contact with condensed water that is generated by the desulfurizing, the cooling, the absorbing of CO 2 , the regenerating, or the washing.
6. The CO 2 recovery method according to claim 5 , wherein the producing of the acid water includes:
measuring a water level of the acid water;
measuring a pH value of the acid water; and
adjusting the water level and the pH value of the acid water by controlling the contact between the exhaust gas and the water according to measurement values for the water level and the pH value of the acid water.
7. The CO 2 recovery method according to claim 5 , wherein the removing includes:
circulating the acid water to be made in contact with the decarbonated exhaust gas;
measuring a pH value of the acid water to be circulated;
supplying new acid water to the circulated acid water according to a measurement value of the pH value of the acid water;
measuring an amount of the new acid water to be supplied; and
controlling the amount of the new acid water to be supplied according to the measurement value of the pH value of the acid water.