Systems and methods for CO
The present disclosure provides improved systems, assemblies and methods to remove and recover CO 2 from emissions. More particularly, the present disclosure provides improved membrane contactors configured to remove CO 2 from flue gas by temperature swing absorption. In exemplary embodiments, the present disclosure provides a novel hollow fiber membrane contactor that integrates absorption and stripping using a nonvolatile reactive absorbent (e.g., 80% polyamidoamine (PAMAM) dendrimer generation 0, and 20% of an ionic liquid (IL)). Equilibrium CO 2 absorption in the nonvolatile viscous mixed absorbent is as high as 6.37 mmolCO 2 /g absorbent in the presence of moisture at 50° C. A novel membrane contactor is provided for CO 2 absorption and stripping via a process identified as temperature swing membrane absorption (TSMAB). The contactor integrates non-dispersive gas absorption and hot water-based CO 2 stripping in one device/assembly containing two sets of commingled hollow fibers.
1. A method to remove CO 2 from emissions comprising:
providing a housing;
disposing a first plurality and a second plurality of hollow fibers in the housing, the first plurality of hollow fibers including porous wall hydrophobic hollow fibers and the second plurality of hollow fibers including solid wall hollow fibers;
disposing an absorbent in the housing between the first and second plurality of hollow fibers;
flowing feed gas through the first plurality of hollow fibers, the first plurality of hollow fibers configured to allow CO 2 from the feed gas to diffuse to and be absorbed in the absorbent;
shutting down the flow of feed gas;
flowing hot water through the second plurality of hollow fibers to heat the absorbent and strip the absorbed CO 2 into the first plurality of hollow fibers; and
withdrawing the stripped CO 2 from the housing through the first plurality of hollow fibers.
2. The method of claim 1 , wherein the feed gas is flowed through the first plurality of hollow fibers at about 50° C.; and
wherein the hot water is flowed through the second plurality of hollow fibers between about 85° C. and about 97° C.
3. The method of claim 1 , wherein after the stripped CO 2 is withdrawn, the method further includes the step of flowing cold water through the second plurality of hollow fibers to cool the absorbent.
4. The method of claim 1 , wherein the absorbent is a substantially pure low molecular weight amine absorbent.
5. The method of claim 1 , wherein the absorbent is selected from the group consisting of methyldiethanolamine, diethanolamine, aMDEA, primary amines, secondary amines, tertiary amines, hindered amines, oligomeric nonvolatile amines, polyamidoamine dendrimer generation 0, and mixtures thereof.
6. The method of claim 1 , wherein the first and second plurality of hollow fibers include polymeric hollow fibers that are commingled with one another within the housing.
7. The method of claim 1 , wherein the second plurality of hollow fibers are substantially impermeable to moisture, CO 2 , N 2 and O 2 .
8. The method of claim 1 , wherein the absorbent includes from about 5% to about 50% water; and
wherein the housing is connected to a reservoir containing additional absorbent.
9. The method of claim 1 , wherein the first plurality of hollow fibers includes hollow fibers having an outer diameter of about 290 μm and an inner diameter of about 240 μm, and having a wall porosity of from about 0.20 to about 0.80; and
wherein the second plurality of hollow fibers includes hollow fibers having an inner diameter between about 250 μm and about 300 gm, and having a solid wall thickness between about 50 μm to about 75 μm.
10. The method of claim 1 , wherein the first plurality of hollow fibers includes hollow fibers having a highly porous superhydrophobic fluorosiloxane coating on the outer diameter of the fibers.
11. A method to remove CO 2 from emissions comprising:
providing a cylindrical housing;
disposing a first plurality and a second plurality of polymeric hollow fibers in the cylindrical housing, the first plurality of polymeric hollow fibers including porous wall hydrophobic hollow fibers and the second plurality of polymeric hollow fibers including solid wall hollow fibers, the first and second plurality of polymeric hollow fibers commingled with one another within the cylindrical housing;
disposing an amine absorbent in the cylindrical housing between the first and second plurality of polymeric hollow fibers;
flowing flue gas through the first plurality of polymeric hollow fibers, the first plurality of polymeric hollow fibers configured to allow CO 2 from the flue gas to diffuse to and be absorbed in the amine absorbent;
shutting down the flow of flue gas;
flowing hot water through the second plurality of polymeric hollow fibers to heat the amine absorbent and strip the absorbed CO 2 into the first plurality of polymeric hollow fibers;
withdrawing the stripped CO 2 from the cylindrical housing through the first plurality of polymeric hollow fibers; and
flowing cold water, after the stripped CO 2 is withdrawn, through the second plurality of polymeric hollow fibers to cool the amine absorbent.