Method for mist control
A method for capturing CO 2 from a CO 2 containing gas ( 1 ), such as en exhaust gas from a thermal power plant fired on carbonaceous fuel, or any other CO 2 containing industrial gas, where CO 2 is captured from the gas by causing the gas to flow counter current to a CO 2 absorbing solvent introduced into a CO 2 absorption section ( 3 ) in an absorber ( 2 ) so that CO 2 present in the gas is absorbed by the CO 2 absorbing solvent to form a CO 2 rich solvent ( 5 ), where CO 2 rich solvent is collected on the bottom of the of the absorption column and withdrawn for regeneration, and where the treated exhaust gas ( 8 ) is released to the atmosphere after being subjected to one or more washing step(s) ( 6,7 ), wherein the temperature of the CO 2 absorbing solvent ( 4 ) introduced into the CO 2 absorption section has a temperature that is less than 5° C. lower than the maximum temperature in the absorption section of the absorber, is described.
1. A method for capturing CO 2 from a CO 2 containing gas, the method comprising:
capturing CO 2 from the CO 2 containing gas by causing the CO 2 containing gas to flow upwards counter current to an aqueous amine solvent flowing once-through downwards in a CO 2 absorption section in an absorber so that CO 2 present in the CO 2 containing gas is absorbed by the aqueous amine solvent to form a CO 2 rich solvent;
wherein the CO 2 rich solvent is collected at a bottom of the absorber and withdrawn for regeneration;
wherein a treated exhaust gas is released to an atmosphere after being subjected to one or more washing step(s) where the treated exhaust gas is washed in counter current flow to water; and
wherein a temperature of the aqueous amine solvent introduced into the CO 2 absorption section is less than or equal to a maximum temperature in the absorption section and not more than 5° C. lower than the maximum temperature in the absorption section of the absorber, thereby reducing amine mist formation.
2. The method of claim 1 , wherein the treated exhaust gas leaving the absorption section is subjected to two or more downstream washing steps where the treated exhaust gas is washed in counter current flow to water and wherein the water introduced into a first washing step has a temperature that is equal to or higher than a wet bulb temperature of a flue gas that is introduced into the washing step.
3. The method of claim 1 , wherein the aqueous amine solvent is introduced into a top of the absorption section at a temperature from 60 to 85° C.
4. The method of claim 3 , wherein the temperature of the aqueous amine solvent introduced into the absorption section is between 70 and 80° C.
5. The method of claim 1 , wherein CO 2 exhausted exhaust gas leaving a second washing section is caused to flow countercurrent to an aqueous acid solution in an acid wash section in order to remove alkaline gaseous compounds such as volatile amines and ammonia, from the exhaust gas.