Apparatus for removing carbon dioxide in combustion exhaust gas
View Patent ↗An object of the present invention is to provide a CO 2 removal apparatus that prevents release of an amine compound of an absorbing solution from a CO 2 absorption device. The CO 2 removal apparatus includes a desorption column 13 that heats and regenerates an amine compound aqueous solution discharged from a decarbonator 1 making counterflow contact of a combustion exhaust gas and an amine compound aqueous solution; and reflux means that refluxes an amine compound aqueous solution regenerated in the desorption column 13 to the decarbonator 1 via a cooler 19 . A contact section that makes counterflow contact of reflux water of the desorption column 13 and a CO 2 -removed combustion exhaust gas is formed in two stages, and the cooler 19 on the downstream side of the desorption column is also formed in two stages. Reflux water from the first stage cooler is supplied to the first stage contact section, and reflux water from the second stage cooler is supplied to the second stage contact section. As a result, the reflux water from the cooler 19 on the downstream side of the desorption column 13 can be efficiently used for amine removal of the decarbonator 1 , and a concentration of an amine released from the decarbonator can be reduced.
1. An apparatus for removing carbon dioxide in a combustion exhaust gas, the apparatus comprising:
a decarbonator comprising a contact section for making counterflow contact of the combustion exhaust gas and an amine compound aqueous solution to remove carbon dioxide from the combustion exhaust gas, a first washing section located downstream of the CO 2 -removed combustion exhaust gas from the contact section, and a second washing section located downstream of the washed combustion exhaust gas from the first washing section;
a desorption column for desorbing CO2 from the amine compound aqueous solution by heating the amine compound aqueous solution discharged from the decarbonator; and
a first cooler located downstream of the desorbed CO 2 discharged from the desorption column to obtain a first reflux water containing a first concentration of the amine compound; and
a second cooler located downstream of the desorbed CO 2 discharged from the first cooler to obtain a second reflux water containing a second concentration of the amine compound;
the first washing section for making counterflow contact of the first reflux water and the CO2-removed combustion exhaust gas from the contact section;
the second washing section for making counterflow contact of the second reflux water and the CO2-removed combustion exhaust gas from the first washing section;
a first pipe arranged from the first cooler to the first washing section to send the first reflux water from the first cooler to the first washing section;
a second pipe arranged from the second cooler to the second washing section to send the second reflux water from the second cooler to the second washing section; and
a third pipe arranged from the second washing section to the first washing section to send a solution in the second washing section from the second washing section to the first washing section;
wherein the first concentration is higher than the second concentration.
2. A method for removing carbon dioxide from a combustion exhaust gas using the apparatus according to claim 1 , comprising:
making counterflow contact of the combustion exhaust gas and an amine compound aqueous solution in the contact section to remove carbon dioxide from the combustion exhaust gas;
washing the CO 2 -removed combustion exhaust gas from the contact section with the first reflux water containing a first concentration of the amine compound in the first washing section;
washing the washed combustion exhaust gas from the first washing section with the second reflux water containing a second concentration of the amine compound in the second washing section;
desorbing CO 2 from the amine compound aqueous solution in the desorption column by heating the amine compound aqueous solution discharged from the decarbonator;
cooling the desorbed CO 2 discharged from the desorption column in the first cooler to obtain the first reflux water;
cooling the desorbed CO2 discharged from the first cooler in the second cooler to obtain the second reflux water;
sending the first reflux water from the first cooler to the first washing section;
sending the second reflux water from the second cooler to the second washing section; and
sending a solution in the second washing section from the second washing section to the first washing section,
wherein the amount of the first reflux water and the second reflux water supplied from the first cooler and the second cooler to the first washing section and the second washing section is adjusted so that a temperature of the combustion exhaust gas in an inlet of the decarbonator is substantially the same as a temperature of the CO 2 -removed combustion exhaust gas in an outlet of the decarbonator; and
wherein the first concentration is higher than the second concentration.