Composite amine absorbing solution, and device and method for removing CO2 or H2S or both
The composite amine absorbing solution according to the present invention absorbs CO 2 or H 2 S or both in a gas, and is obtained by dissolving a linear monoamine, a diamine, and an amide group-containing compound in water. By adopting this composite amine absorbing solution, the composites are interacting in a composite manner, due to an integrated effect of the components, the absorption property of CO 2 or H 2 S or both is favorable, the desorption properties of the CO 2 or H 2 S absorbed when regenerating the absorbing solution become favorable, and the amount of steam from a reboiler used when regenerating the absorbing solution in a CO 2 recovery device can be reduced.
1. A composite amine absorbing solution that absorbs CO 2 or H 2 S or both in a gas, the composite amine absorbing solution comprising:
two kinds of linear monoamine selected from
a combination of a primary linear monoamine having a low steric hindrance and a primary linear monoamine having a high steric hindrance,
a combination of a secondary linear monoamine and a tertiary linear monoamine,
a combination of the primary linear monoamine having a high steric hindrance and the secondary linear monoamine, and
a combination of the primary linear monoamine having a high steric hindrance and the tertiary linear monoamine,
a diamine; and
an amide group-containing compound having a boiling point of 130° C. or higher at an atmospheric pressure and having a dielectric constant of 20 or more at 25° C., wherein
the primary linear monoamine having the low steric hindrance is a compound selected from monoethanolamine (MEA), 3-amino-1-propanol, 4-amino-1-butanol, and diglycolamine,
the primary linear monoamine having the high steric hindrance is a compound selected from 2-amino-1-propanol (2A1P), 2-amino-1-butanol (2A1B), 2-amino-3-methyl-1-butanol (AMB), 1-amino-2-propanol (1A2P), 1-amino-2-butanol (1A2B), and 2-amino-2-methyl-1-propanol (AMP),
a blending ratio of the diamine and the amide group-containing compound with respect to the two kinds of linear monoamine is 0.16 to 2.1,
when the two kinds of linear monoamine are the primary linear monoamine having the low steric hindrance and the primary linear monoamine having the high steric hindrance, a weight ratio of the primary linear monoamine having the high steric hindrance to the primary linear monoamine having the low steric hindrance is between 0.3 to 2.5,
when the two kinds of linear monoamine are the secondary linear monoamine and the tertiary linear monoamine, a weight ratio of the tertiary linear monoamine to the secondary linear monoamine is between 0.3 to 2.5,
when the two kinds of linear monoamine are the primary linear monoamine having the high steric hindrance and the secondary linear monoamine, a weight ratio of the primary linear monoamine having the high steric hindrance to the secondary linear monoamine is between 0.3 to 2.5, and
when the two kinds of linear monoamine are the primary linear monoamine having the high steric hindrance and the tertiary linear monoamine, a weight ratio of the primary linear monoamine having the high steric hindrance to the tertiary linear monoamine is between 0.3 to 2.5.
2. The composite amine absorbing solution according to claim 1 , wherein the diamine includes at least one of a primary linear polyamine, a secondary linear polyamine, and a cyclic polyamine.
3. The composite amine absorbing solution according to claim 1 , wherein a total concentration of the two kinds of linear monoamine and the diamine is 40% to 60% by weight of the entire absorbing solution.
4. The composite amine absorbing solution according to claim 1 , wherein a blending ratio between the diamine and the amide group-containing compound is 1:0.4 to 1:54.
5. A device for removing CO 2 or H 2 S or both, the device comprising:
an absorption tower that brings a gas containing CO 2 or H 2 S or both and an absorbing solution into contact with each other to remove CO 2 or H 2 S or both; and
an absorbing solution regeneration tower that regenerates a solution that has absorbed CO 2 or H 2 S or both,
wherein a solution regenerated by removing CO 2 or H 2 S or both in the absorbing solution regeneration tower is reused in the absorption tower, and the composite amine absorbing solution according to claim 1 is used.
6. The device for removing CO 2 or H 2 S or both according to claim 5 , wherein an absorbing temperature in the absorption tower is 30° C. to 80° C., and a regeneration temperature in the absorbing solution regeneration tower is 110° C. or higher.
7. A method for removing CO 2 or H 2 S or both, the method comprising:
bringing a gas containing CO 2 or H 2 S or both and an absorbing solution into contact with each other to remove CO 2 or H 2 S or both in an absorption tower;
regenerating a solution that has absorbed CO 2 or H 2 S or both in an absorbing solution regeneration tower; and
reusing a solution regenerated by removing CO 2 or H 2 S or both in the absorbing solution regeneration tower, in the absorption tower,
wherein CO 2 or H 2 S or both is removed using the composite amine absorbing solution according to claim 1 .
8. The method for removing CO 2 or H 2 S or both according to claim 7 , wherein an absorbing temperature in the absorption tower is 30° C. to 80° C., and a regeneration temperature in the absorbing solution regeneration tower is 110° C. or higher.