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 CO 2 absorption and stripping system comprising:
a housing;
a first plurality and a second plurality of hollow fibers disposed 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;
an absorbent disposed in the housing between the first and second plurality of hollow fibers;
wherein after feed gas passes through the first plurality of hollow fibers, the first plurality of hollow fibers is configured to allow CO 2 from the feed gas to diffuse to and be absorbed in the absorbent;
wherein after the CO 2 diffuses to and is absorbed in the absorbent, hot water passing through the second plurality of hollow fibers heats the absorbent and strips the absorbed CO 2 into the first plurality of hollow fibers, with the first plurality of hollow fibers configured to allow the stripped CO 2 to be withdrawn through the first plurality of hollow fibers;
wherein the second plurality of hollow fibers includes hollow fibers having an inner diameter between about 250 μm and about 300 μm, and having a solid wall thickness between about 50 μm to about 75 μm.
2. The system of claim 1 , wherein the absorbent is a substantially pure low molecular weight amine absorbent.
3. The system 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.
4. The system of claim 1 , wherein the first and second plurality of hollow fibers include polymeric hollow fibers, and wherein the first and second plurality of hollow fibers are commingled within the housing.
5. The system of claim 1 , wherein the second plurality of hollow fibers are substantially impermeable to moisture, CO 2 , N 2 and O 2 .
6. The system 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.
7. The system 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.
8. A CO 2 absorption and stripping system comprising:
a housing;
a first plurality and a second plurality of hollow fibers disposed 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;
an absorbent disposed in the housing between the first and second plurality of hollow fibers;
wherein after feed gas passes through the first plurality of hollow fibers, the first plurality of hollow fibers is configured to allow CO 2 from the feed gas to diffuse to and be absorbed in the absorbent;
wherein after the CO 2 diffuses to and is absorbed in the absorbent, hot water passing through the second plurality of hollow fibers heats the absorbent and strips the absorbed CO 2 into the first plurality of hollow fibers, with the first plurality of hollow fibers configured to allow the stripped CO 2 to be withdrawn through the first plurality of hollow fibers;
wherein the first plurality of hollow fibers includes hollow fibers having a highly porous superhydrophobic fluorosiloxane coating on the outer diameter of the fibers.
9. The system of claim 8 , wherein the absorbent is a substantially pure low molecular weight amine absorbent.
10. The system of claim 8 , 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.
11. The system of claim 8 , wherein the first and second plurality of hollow fibers include polymeric hollow fibers, and wherein the first and second plurality of hollow fibers are commingled within the housing.
12. The system of claim 8 , wherein the second plurality of hollow fibers are substantially impermeable to moisture, CO 2 , N 2 and O 2 .
13. The system of claim 8 , wherein the absorbent includes from about 5% to about 50% water; and
wherein the housing is connected to a reservoir containing additional absorbent.
14. The system of claim 8 , wherein the first plurality of hollow fibers includes hollow fibers having an outer diameter of about 290 82 m and an inner diameter of about 240 μm, and having a wall porosity of from about 0.20 to about 0.80.