An absorbent regenerator includes: a rich solution supply line; a lean solution supply line; a lean-rich solution heat exchanger that is provided at an intersection of the lean solution supply line and the rich solution supply line; a branch portion that branches some of the rich solution at a downstream side of the lean-rich solution heat exchanger on the rich solution supply line; and a first mixing portion that mixes the some of the rich solution branched at the branch portion with a semi-lean solution, wherein a front end of a branch line through which the some of the branched rich solution is supplied is connected to a solution storage portion of the semi-lean solution which is located at an upper stage side of the absorbent regenerator divided into parts, and the some of the branched rich solution is mixed with the semi-lean solution.
1. A CO 2 recovery unit comprising:
a CO 2 absorber in which a CO 2 -containing gas comes into contact with a CO 2 absorbent to remove CO 2; and
an absorbent regenerator in which a CO 2 -absorbed rich solution is regenerated by a regenerating heater, thereby reusing a lean solution in which CO 2 has been removed in the absorbent regenerator, in the CO 2 absorber as the CO 2 absorbent, wherein
the absorbent regenerator is divided into at least two parts and includes:
a rich solution supply line through which the rich solution is supplied to the absorbent regenerator from the CO 2 absorber;
a lean solution supply line through which the lean solution is supplied to the CO 2 absorber from the absorbent regenerator;
a lean-rich solution heat exchanger that is provided at an intersection of the lean solution supply line and the rich solution supply line to exchange heat between the lean solution and the rich solution;
a branch portion that branches some of the rich solution at a downstream side of the lean-rich solution heat exchanger on the rich solution supply line;
a branch line that branches at the branch portion on the rich solution supply line to supply the some of the rich solution:
a solution storage portion of the semi-lean solution which is located at a bottom of an upper stage side of the absorbent regenerator divided into parts; and
a mixing portion that mixes the some of the rich solution with a semi-lean solution in which CO 2 has been partially removed from the rich solution in the absorbent regenerator,
wherein a front end of the branch line is connected to the solution storage portion of the semi-lean solution to form the mixing portion that mixes the some of the rich solution with the semi-lean solution.
2. A CO 2 recovery unit comprising:
a CO 2 absorber in which a CO 2 -containing gas comes into contact with a CO 2 absorbent to remove CO 2 ; and
an absorbent regenerator in which a CO 2 -absorbed rich solution is regenerated by a regenerating heater, thereby reusing a lean solution in which CO 2 has been removed in the absorbent regenerator, in the CO 2 absorber as the CO 2 absorbent, wherein
the absorbent regenerator is divided into at least two parts and includes:
a rich solution supply line through which the rich solution is supplied to the absorbent regenerator from the CO 2 absorber;
a lean solution supply line through which the lean solution is supplied to the CO 2 absorber from the absorbent regenerator;
a lean-rich solution heat exchanger that is provided at an intersection of the lean solution supply line and the rich solution supply line to exchange heat between the lean solution and the rich solution;
a branch portion that branches some of the rich solution at a downstream side of the lean-rich solution heat exchanger on the rich solution supply line;
a branch line that branches at the branch portion on the rich solution supply line to supply the some of the rich solution;
a solution storage portion of the semi-lean solution which is located at a bottom of an upper stage side of the absorbent regenerator divided into parts;
a line mixing portion that mixes the some of the rich solution with a semi-lean solution in which CO 2 has been partially removed from the rich solution in the absorbent regenerator; and
a semi-lean solution extracting line that extracts the semi-lean solution from the solution storage portion of the semi-lean solution and to be supplied to a lower stage side of the absorbent regenerator,
wherein a front end of the branch line is directly connected with the semi-lean solution extracting line to form the line mixing portion that mixes the some of the rich solution with the semi-lean solution.
3. The CO 2 recovery unit according to claim 2 , wherein
at an upstream side of the lean-rich solution heat exchanger interposed on the lean solution supply line, a lean and semi-lean solution heat exchanger is provided at an intersection of the lean solution supply line and the semi-lean solution extracting line, and
after the some of the branched rich solution and the semi-lean solution are mixed with each other in the mixing portion, the mixed solution exchanges heat with the lean solution in the lean and semi-lean solution heat exchanger.
4. The CO 2 recovery unit according to claim 3 , comprising a steam condensate heat exchanger that is interposed at a downstream side of the mixing portion on the semi-lean solution extracting line to heat the mixed solution of the some of the branched rich solution and the semi-lean solution using residual heat of steam condensate from a regenerating heater of the absorbent regenerator.