A CO 2 recovery system includes an absorption tower and a regeneration tower. CO 2 rich solution is produced in the absorption tower by absorbing CO 2 from CO 2 -containing gas. The CO 2 rich solution is conveyed to the regeneration tower where lean solution is produced from the rich solution by removing CO 2 . A regeneration heater heats lean solution that accumulates near a bottom portion of the regeneration tower with saturated steam thereby producing steam condensate from the saturated steam. A steam-condensate heat exchanger heats the rich solution conveyed from the absorption tower to the regeneration tower with the steam condensate.
1. A CO 2 recovery method including causing CO 2 -containing gas to come in contact with CO 2 -absorbing solution to produce CO 2 rich solution in an absorption tower, conveying the rich solution to a regeneration tower including an upper-portion regeneration tower and a lower-portion regeneration tower, and producing a lean solution from the rich solution by removing CO 2 from the rich solution in the regeneration tower,
the CO 2 recovery method comprising:
extracting lean solution that accumulates near a bottom portion of the regeneration tower, heating extracted lean solution with saturated steam to produce steam condensate from the saturated steam, and returning the extracted lean solution after heating the saturated steam to the regeneration tower;
obtaining a semi-lean solution from the upper-portion regeneration tower;
branching the rich solution into first and second rich solution parts;
heat-exchanging the first rich solution part with the steam condensate;
heat-exchanging the second rich solution part with the semi-lean solution;
conveying the heat-exchanged first rich solution part to the lower-portion regeneration tower; and
conveying the heat-exchanged second rich solution part to the upper-portion regeneration tower.
2. A CO 2 recovery method including causing CO 2 -containing gas to come in contact with CO 2 -absorbing solution to produce CO 2 rich solution in an absorption tower, conveying the rich solution to a regeneration tower including an upper-portion regeneration tower and a lower-portion regeneration tower, and producing a lean solution from the rich solution by removing CO 2 from the rich solution in the regeneration tower,
the CO 2 recovery method comprising:
extracting lean solution that accumulates near a bottom portion of the regeneration tower, heating extracted lean solution with saturated steam to produce steam condensate from the saturated steam, and returning the extracted lean solution after heating the saturated steam to the regeneration tower;
extracting semi-lean solution from a middle portion of the regeneration tower;
branching the extracted semi-lean solution into first and second semi-lean solution parts;
heat-exchanging the first semi-lean solution part with the steam condensate, and returning the first semi-lean solution part that has been heated by the saturated steam to the regeneration tower;
conveying the second semi-lean solution part to a middle stage portion of the absorption tower;
branching the rich solution from the absorption tower into first and second rich solution parts;
heat-exchanging the first rich solution part with the lean solution;
heat-exchanging the second rich solution part with the extracted semi-lean solution;
adding the heat-exchanged second rich solution part to the heat-exchanged first rich solution part so as to obtain as a mixed rich solution; and
heat-exchanging the mixed rich solution with the lean solution from the regeneration tower.
3. A CO 2 recovery method including causing CO 2 -containing gas to come in contact with CO 2 -absorbing solution to produce CO 2 rich solution in an absorption tower, conveying the rich solution to a regeneration tower, and producing a lean solution from the rich solution by removing CO 2 from the rich solution in the regeneration tower, the CO 2 recovery method comprising:
performing transfer of heat from lean solution to semi-lean solution obtained by removing part of CO 2 from the rich solution, the semi-lean solution having been extracted from a middle portion of the regeneration tower;
extracting semi-lean solution from a middle portion of the regeneration tower, heating extracted semi-lean solution with lean solution extracted from the regeneration tower, returning the extracted semi-lean solution that has been heated by the lean solution to the regeneration tower, and conveying the lean solution after heating the semi-lean solution to the absorption tower.