Carbon dioxide separating and capturing apparatus and method of operating same

1. A carbon dioxide separating and capturing apparatus comprising:

an absorption tower to which a gas containing carbon dioxide is introduced, the absorption tower being configured to allow the gas to contact with an absorption liquid for absorbing the carbon dioxide, and to discharge a rich liquid which is the absorption liquid having absorbed the carbon dioxide;

a regeneration tower configured to heat the absorption liquid to cause the absorption liquid to release a gas containing the carbon dioxide, and to discharge a lean liquid having a concentration of dissolved carbon dioxide which is lower than a concentration of dissolved carbon dioxide in the rich liquid; and

first and second regenerative heat exchangers configured to heat the rich liquid by using the lean liquid,

wherein

the first regenerative heat exchanger is a heat exchanger of plate type, heats the rich liquid discharged from the absorption tower by using the lean liquid discharged from the second regenerative heat exchanger, and discharges the rich liquid in a liquid phase,

the second regenerative heat exchanger is a heat exchanger of shell-and-tube type, heats the rich liquid in the liquid phase discharged from the first regenerative heat exchanger by using the lean liquid discharged from the regeneration tower, and causes the rich liquid to generate a steam and to release a carbon dioxide gas,

the lean liquid discharged from the first regenerative heat exchanger is fed to the absorption tower, and

the rich liquid, the steam and the carbon dioxide gas discharged from the second regenerative heat exchanger is fed to the regeneration tower,

the apparatus further comprising:

a first measuring device configured to measure the concentration of the dissolved carbon dioxide in the rich liquid fed to the first regenerative heat exchanger;

a second measuring device configured to measure a temperature of the rich liquid discharged from the first regenerative heat exchanger;

a third measuring device configured to measure a pressure of the rich liquid discharged from the first regenerative heat exchanger;

a pressure adjusting valve configured to adjust the pressure of the rich liquid discharged from the first regenerative heat exchanger; and

a controller configured to calculate, by using the values of the first and second measuring devices and gas-liquid equilibrium data of the absorption liquid, a pressure value at which the rich liquid discharged from the first regenerative heat exchanger maintains it in the liquid phase, and to control the pressure adjusting valve so that a measurement result of the third measuring device is equal to or greater than the calculated pressure value.

2. The apparatus of claim 1 , further comprising a flow divider configured to divide the rich liquid discharged from the absorption tower into a first rich liquid and a second rich liquid,

wherein

the first rich liquid is fed to the first regenerative heat exchanger, and

the second rich liquid is heated with a gas containing the carbon dioxide discharged from the regeneration tower.

3. The apparatus of claim 1 , wherein the second regenerative heat exchanger is a heat exchanger of kettle reboiler type.

4. A method of operating a carbon dioxide separating and capturing apparatus including an absorption tower, a regeneration tower, a first regenerative heat exchanger of plate type, and a second regenerative heat exchanger of shell-and-tube type, the method comprising:

allowing a gas containing carbon dioxide to contact with a lean liquid discharged from the first regenerative heat exchanger in the absorption tower, and discharging a rich liquid which is the absorption liquid having absorbed carbon dioxide from the absorption tower;

heating the rich liquid discharged from the absorption tower by using the lean liquid discharged from the second regenerative heat exchanger in the first regenerative heat exchanger, and discharging the rich liquid in a liquid phase;

heating the rich liquid in the liquid phase discharged from the first regenerative heat exchanger by using the lean liquid discharged from the regeneration tower in the second regenerative heat exchanger, and allowing the rich liquid to generate a steam and to release a carbon dioxide gas;

feeding the rich liquid, the steam and the carbon dioxide gas discharged from the second regenerative heat exchanger to the regeneration tower to cause the rich liquid to release a gas containing the carbon dioxide, and discharging the lean liquid having a concentration of dissolved carbon dioxide which is lower than a concentration of dissolved carbon dioxide in the rich liquid;

measuring, by using a first measuring device, the concentration of the dissolved carbon dioxide in the rich liquid fed to the first regenerative heat exchanger;

measuring, by using a second measuring device, a temperature of the rich liquid discharged from the first regenerative heat exchanger;

measuring, by using a third measuring device, a pressure of the rich liquid discharged from the first regenerative heat exchanger;

calculating, by using the values of the first and second measuring devices and gas-liquid equilibrium data of the absorption liquid, a pressure value at which the rich liquid discharged from the first regenerative heat exchanger maintains it in the liquid phase; and

controlling a pressure adjusting valve configured to adjust the pressure of the rich liquid discharged from the first regenerative heat exchanger so that a measurement result of the third measuring device is equal to or greater than the calculated pressure value.