Biocatalyst-based CO
A method for stripping CO 2 from a biocatalyst-containing CO 2 -rich absorption solution to produce a biocatalyst-containing CO 2 -lean absorption solution and a CO 2 -rich gas is provided. The method includes generating a stripping gas from a portion of the biocatalyst-containing CO 2 -lean absorption solution in a stripping gas generation unit, and contacting the biocatalyst-containing CO 2 -rich absorption solution with the stripping gas in a gas-liquid contactor to produce the CO 2 -lean absorption solution and the CO 2 -rich gas.
1 . A method for stripping CO 2 from a biocatalyst-containing CO 2 -rich absorption solution to produce a biocatalyst-containing CO 2 -lean absorption solution and a CO 2 -rich gas, the method comprising:
generating a stripping gas from a portion of the biocatalyst-containing CO 2 -lean absorption solution in a stripping gas generation unit, and
contacting the biocatalyst-containing CO 2 -rich absorption solution with the stripping gas in a gas-liquid contactor to produce the CO 2 -lean absorption solution and the CO 2 -rich gas;
wherein the biocatalyst is a carbonic anhydrase in a soluble form, freely dissolved in the absorption solution such that the carbonic anhydrase in a soluble form flows in solution within the stripping gas generation unit and is maintained in soluble form throughout the flow of the absorption solution in the stripping gas generation unit, and wherein the stripping gas generation unit is a falling film evaporator.
2 . The method of claim 1 , wherein the gas-liquid contactor is a gas-liquid direct contactor.
3 . The method of claim 2 , wherein the gas-liquid contactor is a packed column, a tray column, a spray reactor or a rotating packed bed.
4 . A method for stripping CO 2 from a biocatalyst-containing CO 2 -rich absorption solution to produce a biocatalyst-containing CO 2 -lean absorption solution and a CO 2 -rich gas, the method comprising:
generating a stripping gas from the biocatalyst-containing CO 2 -rich absorption solution, and
contacting the biocatalyst-containing CO 2 -rich absorption solution with the stripping gas in a gas-liquid contactor to produce the CO 2 -lean absorption solution and the CO 2 -rich gas;
wherein the biocatalyst is a carbonic anhydrase in a soluble form, freely dissolved in the absorption solution such that the carbonic anhydrase in a soluble form flows in solution within the stripping gas generation unit and is maintained in soluble form throughout the flow of the absorption solution in the stripping gas generation unit, and wherein the stripping gas generation unit is a falling film evaporator.
5 . The method of claim 4 , wherein generating the stripping gas comprises heating the biocatalyst-containing CO 2 -rich absorption solution in the gas-liquid contactor, thereby simultaneously generating the stripping gas and stripping CO 2 from the biocatalyst-containing CO 2 -rich absorption solution in the gas-liquid contactor.
6 . The method of claim 4 , wherein the gas-liquid contactor is a gas-liquid direct contactor, optionally a falling film evaporator.
7 . The method of claim 1 , wherein the biocatalyst-containing CO 2 -rich absorption solution is an aqueous solution, and the generated stripping gas includes steam.
8 . The method of claim 1 , wherein the stripping gas is fed to a plurality of spaced-apart locations distributed along a height of the gas-liquid contactor.
9 . The method of claim 1 , wherein the biocatalyst-containing CO 2 -rich absorption solution is withdrawn from different sections of the gas-liquid contactor to be heated and reinjected in the gas-liquid contactor via heating loops.
10 . The method of claim 1 , comprising minimizing or avoiding exposure of the biocatalyst-containing CO 2 -rich absorption solution and the biocatalyst-containing CO 2 -lean absorption solution to bubble-formation conditions at which new gas-liquid interfaces are created via bubble formation.
11 . A biocatalyst-based CO 2 capture process comprising:
contacting a CO 2 -containing gas with a biocatalyst-containing absorption solution to produce a biocatalyst-containing CO 2 -rich absorption solution, and
using a CO 2 stripping method as defined in claim 1 to desorb CO 2 from the biocatalyst-containing CO 2 -rich absorption solution, thereby producing the CO 2 -lean absorption solution and the CO 2 -rich gas;
wherein the biocatalyst is a carbonic anhydrase in a soluble form, freely dissolved in the absorption solution such that the carbonic anhydrase in a soluble form flows in solution within the stripping gas generation unit and is maintained in soluble form throughout the flow of the absorption solution in the stripping gas generation unit, and wherein the stripping gas generation unit is a falling film evaporator.
12 . The method of claim 4 , wherein the biocatalyst-containing CO 2 -rich absorption solution is an aqueous solution, and the generated stripping gas includes steam.
13 . The method of claim 4 , wherein the stripping gas is fed to a plurality of spaced-apart locations, preferably distributed along a height of the gas-liquid contactor.
14 . The method of claim 4 , wherein the biocatalyst-containing CO 2 -rich absorption solution is withdrawn from different sections of the gas-liquid contactor to be heated and reinjected in the gas-liquid contactor via heating loops.
15 . The method of claim 5 , comprising minimizing or avoiding exposure of the biocatalyst-containing CO 2 -rich absorption solution and the biocatalyst-containing CO 2 -lean absorption solution to bubble-formation conditions at which new gas-liquid interfaces are created via bubble formation.