Methods and systems for gas filtering and carbon dioxide capture
View Patent ↗Conventionally air filters are particulate filters composed of fibrous materials in order to remove solid particulates such as dust, pollen, mold, and bacteria from the air. Accordingly, it would be beneficial to provide absorbent filters within such systems in order to address the removal of gaseous impurity components from the circulating air in addition to conventional particulate filters. It would be further beneficial to provide such absorbent filters in a manner which is compatible with commercial and residential environments that represent the majority of such air circulation systems. It would be further beneficial to provide such absorbent filters in formats that are compatible with new system installations as well as retrofitting to existing system installations.
1. A system for filtering a predetermined impurity from a fluid comprising:
a chamber comprising:
an inlet port for receiving the fluid which is to be coupled via the chamber to an outlet port, the inlet port comprising a fluid conduit which has a partition physically dividing the fluid conduit into a first predetermined portion coupled to the chamber and a second predetermined portion coupled to a director such that the fluid flowing within the fluid conduit is divided into a first predetermined fluid portion coupled into the chamber and a second predetermined fluid portion coupled to the director;
the outlet port;
a reservoir within the chamber to be filled above a predetermined depth with a mixture of an absorber established in dependence upon the predetermined impurity and a solvent;
an absorber duct disposed within the chamber between the inlet port and outlet port covering a predetermined portion of the chamber between the inlet port and the outlet port and comprising:
an opening at the bottom of the absorber duct disposed within the reservoir such that the opening is below a predetermined distance from the bottom of the reservoir and is coupled to a distal end of the director from the fluid conduit;
a permeable membrane forming a predetermined portion of the absorber duct such that the first predetermined fluid portion flows through the permeable membrane, the permeable membrane permeable to the fluid and the predetermined impurity; and
the director coupled between the second predetermined portion of the fluid conduit and the opening at the bottom of the absorber duct inlet port for directing the second predetermined fluid portion from the fluid conduit to the opening at the bottom of the absorber duct within the reservoir;
wherein
when the reservoir is filled with the mixture to at least the predetermined depth and the fluid flows into the inlet port the portion of the absorber duct filled with the mixture increases in dependence upon the fluid flow rate at the inlet port; and
when the reservoir is filled with the mixture to at least the predetermined depth and the fluid flows into the inlet port the portion of the first predetermined fluid portion flowing through the mixture within the absorber duct increases in dependence upon the fluid flow rate at the inlet port.
2. The system according to claim 1 , wherein
the absorber within the mixture removes the predetermined impurity from the fluid.
3. The system according to claim 1 , wherein
the mixture comprises a calcium hydroxide solution; and
the predetermined impurity is at least one of carbon dioxide and sulphur dioxide.
4. The system according to claim 1 , wherein
the absorber duct fills the chamber laterally and vertically above the predetermined depth in the reservoir such that all of the first predetermined fluid portion must flow via the permeable membrane.
5. The system according to claim 1 , wherein
the first predetermined fluid portion cannot flow from the input port to the output port when the second fluid is filled to the predetermined depth without flowing through the permeable membrane.
6. The system according to claim 1 , wherein
the mixture is added to the reservoir through a first port on an upper surface of the chamber; and
the mixture can be removed from the reservoir through a second port on a lower surface of the chamber.
7. The system according to claim 1 , wherein
the predetermined depth of the mixture allows an inner portion of the absorber duct to be filled with the mixture to its maximum height at the upper maximum fluid flow rate defined for the chamber.
8. The system according to claim 1 , wherein
the absorber duct is replaceable.
9. The system according to claim 1 , wherein
the inlet port and outlet port are coupled to a fluidic circuit.
10. The system according to claim 1 , wherein
the mixture is circulated into and from the reservoir by an external fluidic circuit.
11. The system according to claim 1 , wherein
the permeable membrane is a particulate filter.
12. The system according to claim 1 , wherein
the permeable membrane is not permeable to the mixture.