Efficient and fully automated catalytic direct carbon dioxide capture from air system
An efficient low-energy carbon dioxide removal system comprises an automated air mover equipped with sensing devices to measure flow rate, volume, level, pressure, temperature and concentration. Packing materials and air-liquid distributors are used in a multi-stage catalytic reactor. The multi-stage catalytic reactor processes ambient air and generates pure carbon dioxide gas and generates exhausted gas released to ambient air. In operation, air contacts the base solution in the presence of a catalyst via the air mover, distributor, and packing materials. The air reacts with the base solution thereby generating a base solution having carbon dioxide and generating exhaust (absorption reaction). Next, the exhaust is released from the reactor. Next, a catalyst is added, heat is applied to the base solution having carbon dioxide thereby generating carbon dioxide and generating a base solution without carbon dioxide (desorption reaction).
1. A method comprising:
generating airflow over a packing material and out to ambient air;
continuously coating the packing material with a base medium until the base medium acquires a first concentration of carbon dioxide;
heating the base medium having the first concentration of carbon dioxide to remove the carbon dioxide, wherein air flowing along an output side of the packing material has less carbon dioxide than air flowing along an input side of the packing material; and
compressing the carbon dioxide removed from the base medium.
2. The method of claim 1 , wherein the method directly captures carbon dioxide from ambient air as a feedstock, wherein airflow is generated from ambient in a non-point source capture environment, and wherein the operation of generating the airflow comprises generating the airflow using an element selected from a group consisting of: a compressor, a blower, a fan, a turbofan, a pump, a diaphragm pump, an air contactor, a falling-film evaporator, and an absorber.
3. The method of claim 1 , wherein the operation of continuously coating comprises evenly distributing the base medium over the packing material.
4. The method of claim 1 , further comprising:
measuring the first concentration of carbon dioxide in situ using one or more automated sensing devices that measure conversion efficiency, flow rate, pressure, temperature, and carbon dioxide concentration in both the airflow and exhaust air from the packing material.
5. The method of claim 1 , further comprising:
maintaining the base medium in a collection reservoir;
distributing the base medium from the collection reservoir to continuously coat the packing material; and
collecting excess amounts of the base medium from the packing material in the collection reservoir.
6. The method of claim 5 , wherein the operation of heating further comprises:
generating a selected portion of the base medium having a concentration of carbon dioxide that is less than the first concentration of carbon dioxide; and
returning the selected portion of the base medium to the collection reservoir.
7. The method of claim 6 , wherein the operation of heating further comprises:
collecting the base medium having the first concentration of carbon dioxide in a desorption chamber;
applying a catalyst to the desorption chamber; and
heating the desorption chamber to extract the carbon dioxide and generate the selected portion of the base medium having a concentration of carbon dioxide that is less than the first concentration of carbon dioxide.
8. The method of claim 7 , further comprising:
generating the catalyst to have a general structure of M(O) x (OH) y with 0.1-5 wt % concentration that lowers activation energy of a desorption reaction so that the desorption reaction can be performed at or below 95° C.
9. The method of claim 7 , wherein the operation of heating the desorption chamber comprises:
increasing a chamber temperature to less than 130° C.
10. The method of claim 1 , further comprising:
supplying the carbon dioxide that is removed to a sequestration system or to a low global warming refrigerant generation system.
11. The method of claim 1 , wherein an absorption reaction occurs when the air flow contacts the base medium and the desorption reaction occurs when heat is applied to the base medium having the first concentration of carbon dioxide, and wherein the absorption reaction and desorption reaction are reversible reactions.
12. The method of claim 1 , further comprising:
generating the base medium to comprise a mixture of water and solvents containing a base having at least one of sodium carbonate, potassium carbonate, and lithium carbonate, along with dissolved salts of amino acids of Glycine, Proline, Arginine, Guanidine, and Melamine as catalyst or promoter.
13. The method of claim 1 , further comprising:
generating the base medium to comprise a phase transfer catalyst with a quaternary ammonium cation and a hydroxyl anion with the structure of the form c[M + ]d[Y − ] that reduces interfacial surface tension between air bubble and water mist and promotes mixing in gas-liquid or gas-liquid-solid systems, wherein M is the cation species, wherein Y is the anion species, and wherein c and d are integers such that the total charge is neutral.
14. The method of claim 1 , further comprising:
generating the base medium to comprise corrosion inhibitors, additives, or promoters, wherein the corrosion inhibitors include vanadium pentoxide or other metallic oxides, and wherein the additives or promoters include MEA (monoethanolamine), DEA (diethanolamine), Ethylene Diamine, TEA (triethanolamine), MDEA (methyl diethanolamine), piperazine, glycine, or any material that lowers an activation energy.
15. A method comprising:
generating airflow over a packing material and out to ambient air;
continuously coating the packing material with a base medium until the base medium acquires a first concentration of carbon dioxide;
heating the base medium having the first concentration of carbon dioxide to remove the carbon dioxide, wherein air flowing along an output side of the packing material has less carbon dioxide than air flowing along an input side of the packing material;
maintaining the base medium in a collection reservoir;
distributing the base medium from the collection reservoir to continuously coat the packing material;
collecting excess amounts of the base medium from the packing material in the collection reservoir;
capturing a portion of the base medium from air flowing out from the packing material; and
returning the portion of the base medium to the collection reservoir.
16. An apparatus comprising:
an air mover that generates airflow over a packing material;
a pump that continuously coats the packing material with a base medium until the base medium acquires a first concentration of carbon dioxide;
a heated reservoir that heats the base medium having the first concentration of carbon dioxide to remove the carbon dioxide; and
a compression system that compresses the carbon dioxide removed from the base medium.
17. The apparatus of claim 16 , wherein the air mover is selected from a group consisting of: a compressor, a blower, a fan, a turbofan, a pump, a diaphragm pump, an air contactor, a falling-film evaporator, and an absorber.
18. The apparatus of claim 16 , further comprising:
a distributor that evenly distributes the base medium over the packing material.
19. The apparatus of claim 16 , further comprising:
a processor configured to measure the first concentration of carbon dioxide using one or more automated sensing devices that measure conversion efficiency, flow rate, pressure, temperature, and carbon dioxide concentration in both the airflow and exhaust air from the packing material.
20. The apparatus of claim 19 , wherein the processor performs operations of:
maintaining the base medium in a collection reservoir;
distributing the base medium from the collection reservoir to continuously coat the packing material; and
collecting excess amounts of the base medium from the packing material in the collection reservoir.
21. The apparatus of claim 16 , wherein the heated reservoir performs operations of:
generating a selected portion of the base medium having a concentration of carbon dioxide that is less then the first concentration of carbon dioxide; and
returning the selected portion of the base medium to the collection reservoir.
22. The apparatus of claim 16 , wherein the heated reservoir performs operations of:
collecting the base medium having the first concentration of carbon dioxide;
applying a catalyst to the base medium having the first concentration of carbon dioxide; and
heating the base medium and catalyst to extract the carbon dioxide and generate the selected portion of the base medium having a concentration of carbon dioxide that is less then the first concentration of carbon dioxide.
23. The apparatus of claim 22 , wherein the catalyst has a general structure of M(O) x (OH) y with 0.1-5 wt % concentration that lowers activation energy of a desorption reaction so that the desorption reaction can be performed at or below 95° C.
24. The apparatus of claim 16 , wherein temperature of the heated reservoir is increased to less than 130° C.
25. The apparatus of claim 16 , wherein the airflow has a concentration of carbon dioxide between 0-100% and an exhaust of air from the packing material has a lower concentration of carbon dioxide.
26. The apparatus of claim 16 , wherein an absorption reaction occurs when the airflow contacts the base medium, wherein a desorption reaction occurs when heat is applied to the base medium having the first concentration of carbon dioxide, and wherein the absorption reaction and desorption reaction are reversible reactions.
27. The apparatus of claim 16 , wherein the base medium comprises a mixture of water and solvents containing a base having at least one of sodium carbonate, potassium carbonate, and lithium carbonate, along with dissolved salts of amino acids of Glycine, Proline, Arginine, Guanidine, and Melamine as catalyst or promoter.
28. The apparatus of claim 16 , wherein the base medium comprises a phase transfer catalyst with a quaternary ammonium cation and a hydroxyl anion with the structure of the form c[M + ]d[Y − ] that reduces interfacial surface tension between air bubble and water mist and promotes mixing in gas-liquid or gas-liquid-solid systems, wherein M is the cation species, wherein Y is the anion species, and wherein c and d are integers such that the total charge is neutral.
29. The apparatus of claim 16 , wherein the base medium comprises corrosion inhibitors, additives, or promoters, wherein the corrosion inhibitors include vanadium pentoxide or other metallic oxides, and wherein the additives or promoters include MEA (monoethanolamine), DEA (diethanolamine), Ethylene Diamine, TEA (triethanolamine), MDEA (methyl diethanolamine), piperazine, glycine, or any material that lowers the activation energy.
30. An apparatus comprising:
an air mover that generates airflow over a packing material;
a pump that continuously coats the packing material with a base medium until the base medium acquires a first concentration of carbon dioxide;
a heated reservoir that heats the base medium having the first concentration of carbon dioxide to remove the carbon dioxide;
a processor configured to measure the first concentration of carbon dioxide using one or more automated sensing devices that measure conversion efficiency, flow rate, pressure, temperature, and carbon dioxide concentration in both the airflow and exhaust air from the packing material, wherein the processor performs operations of:
maintaining the base medium in a collection reservoir;
distributing the base medium from the collection reservoir to continuously coat the packing material; and
collecting excess amounts of the base medium from the packing material in the collection reservoir; and
a condenser that captures a portion of the base medium from exhaust air flowing from the packing material, and returns the portion of the base medium to the collection reservoir.