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 system including an absorption tower that receives CO 2 -containing gas and CO 2 -absorbing solution, and causes the CO 2 -containing gas to come in contact with the CO 2 -absorbing solution to produce CO 2 rich solution, and a regeneration tower that receives the rich solution and produces lean solution from the rich solution by removing CO 2 from the rich solution, the CO 2 recovery system comprising:
a bottom lean-solution extraction path that extracts lean solution that accumulates near a bottom portion of the regeneration tower from a first point of the regeneration tower and returns extracted lean solution to a second point of the regeneration tower that is downstream of the first point;
a regeneration heater arranged in the bottom lean-solution extraction path and heats the lean solution in the bottom lean-solution extraction path with saturated steam thereby producing steam condensate from the saturated steam; and
a steam-condensate heat exchanger that heats, with the steam condensate, any one of
the rich solution that is supplied from the absorption tower to the regeneration tower, and
a semi-lean solution that is extracted outside from a middle portion of the regeneration tower and returned to the middle portion of the regeneration tower.
2. The CO 2 recovery system according to claim 1 , wherein the regeneration tower including an upper-portion regeneration tower and a lower-portion regeneration tower, and the CO 2 recovery system further comprising an upper semi-lean-solution extraction path that extracts semi-lean solution from a fifth point of the upper-portion regeneration tower and returns extracted semi-lean solution to a sixth point of the upper-portion regeneration tower that is downstream of the fifth point, wherein
the steam-condensate heat exchanger is arranged in the upper semi-lean-solution extraction path and heats the semi-lean solution in the upper semi-lean-solution extraction path with the steam condensate.