A CO 2 recovering apparatus according to this embodiment includes a cooling tower; a CO 2 absorber, a regenerator; an absorbing solution level meter for measuring the amount of liquid at a tower bottom of the CO 2 absorber; and a level controller for performing automatic control or manual control for one or both of a supply amount of makeup water and a condensation amount of water contained in an exhaust gas based on the liquid amount of at the bottom of the CO 2 absorber detected by the absorbing solution level meter.
1. An operation control method of a CO 2 recovering apparatus comprising:
a CO 2 absorber including a CO 2 recovering unit that brings an exhaust gas containing CO 2 into contact with water to cool the exhaust gas and brings the exhaust gas into contact with a CO 2 absorbing solution absorbing CO 2 to eliminate CO2 contained in the exhaust gas; and
a regenerator that eliminates CO 2 contained in the CO 2 absorbing solution having absorbed CO 2 to regenerate the CO 2 absorbing solution,
the operation control method comprising:
recycling, by the CO 2 absorber, the CO 2 absorbing solution obtained by eliminating CO 2 by the regenerator;
measuring, by an absorbing solution level meter, a liquid level of the CO 2 absorbing solution at a tower bottom of the CO 2 absorber; and
performing, by a level controller, one of automatic control and manual control for one or both of a supply amount of makeup water to be supplied to the CO 2 absorber and a condensation amount of water contained in the exhaust gas, based on the liquid level of the CO 2 absorbing solution detected by the absorbing solution level meter,
wherein the level controller is switched to the automatic control while a change in the gas supply amount of the exhaust gas to be supplied to the CO 2 absorber is finished, and the level controller is switched to the manual control while the gas supply amount of the exhaust gas to be supplied to the CO 2 absorber is changed, to thereby maintain, at a constant level, one or both of the supply amount of the makeup water and the condensation amount of water contained in the exhaust gas.
2. The operation control method according to claim 1 , wherein when a change in the gas supply amount of the exhaust gas supplied to the CO 2 absorber is constant and the level controller is switched from the manual control to the automatic control, measured values of the liquid level of the CO 2 absorbing solution at the tower bottom of the CO 2 absorber, the supply amount of the makeup water, the accumulation amount of the CO 2 absorbing solution, and the gas supply amount of the exhaust gas are changed to set values which are reference values for the measured values.
3. An operation control method of a CO 2 recovering apparatus comprising:
a CO 2 absorber including a CO 2 recovering unit that brings an exhaust gas containing CO 2 into contact with water to cool the exhaust gas and brings the exhaust gas into contact with a CO 2 absorbing solution to eliminate CO 2 contained in the exhaust gas; and
a regenerator that eliminates CO 2 contained in the CO 2 absorbing solution having absorbed CO 2 to regenerate the CO 2 absorbing solution,
the operation control method comprising:
recycling, by the CO 2 absorber, the CO 2 absorbing solution obtained by eliminating CO 2 by the regenerator;
measuring, by an absorbing solution level meter, a liquid level of the CO 2 absorbing solution at a tower bottom of the CO 2 absorber; and
performing, by a level controller, one of automatic control and manual control for one or both of a supply amount of makeup water to be supplied to the CO 2 absorber and a condensation amount of water contained in the exhaust gas, based on the liquid level of the CO 2 absorbing solution detected by the absorbing solution level meter; wherein
while a gas supply amount of the exhaust gas to be supplied to the CO 2 absorber is changed, one of the gas supply amount of the exhaust gas to be supplied to the CO 2 absorber and a load of an apparatus that generates the exhaust gas is applied to a relationship between one of the preliminarily obtained gas supply amount of the exhaust gas and the load of the apparatus that generates the exhaust gas, and a set value of the liquid level of the CO 2 absorbing solution at the bottom of the CO 2 absorber detected by the absorbing solution level meter, and wherein
the level controller controls the set value of one or both of the supply amount of the makeup water and the condensation amount of water contained in the exhaust gas.
4. The operation control method according to claim 3 , wherein the condensation amount of water contained in the exhaust gas is adjusted by using one or both of a method of changing a cooling ratio of the exhaust gas by the cooling tower, and a method of changing a cooling temperature of the CO 2 absorbing solution within the CO 2 absorber.
5. The operation control method according to claim 3 , further comprising:
extracting the CO 2 absorbing solution at the bottom of the CO 2 absorber depending on a loading state of the apparatus that generates the exhaust gas;
storing the extracted CO 2 absorbing solution, or feeding the stored CO 2 absorbing solution to the bottom of the CO 2 absorber; and
adjusting a liquid amount of the CO 2 absorbing solution at the bottom of the CO 2 absorber.
6. The operation control method claim 1 , wherein the condensation amount of water contained in the exhaust gas is adjusted by using one or both of a method of changing a cooling ratio of the exhaust gas by the cooling tower, and a method of changing a cooling temperature of the CO 2 absorbing solution within the CO 2 absorber.
7. The operation control method claim 1 , further comprising:
extracting the CO 2 absorbing solution at the bottom of the CO 2 absorber depending on a loading state of the apparatus that generates the exhaust gas;
storing the extracted CO 2 absorbing solution, or feeding the stored CO 2 absorbing solution to the bottom of the CO 2 absorber; and
adjusting a liquid amount of the CO 2 absorbing solution at the bottom of the CO 2 absorber.