Removal of ozone from electrokinetic devices
Electrokinetic devices and methods are described with the purpose of propelling a dielectric fluid medium, usually air, and optionally collecting assayable agents from the medium. Electrokinetic flow may be induced by the use of plasma generation at high voltage electrodes and consequent transport of charged particles in an electric voltage gradient. The generation of electrokinetic flow has the disadvantage that certain amounts of ozone may be formed in the process. Methods and devices are described herein where suitable catalysts can be combined with the electrokinetic device in such a way that ozone is effectively destroyed in the effluent flow without compromising the amount of flow.
1. An electrokinetic air propulsion device, comprising:
a housing having an inlet and an outlet;
a high voltage electrode and a propulsion electrode in said housing adapted to generate air flow in the housing from the inlet to the outlet; and
a porous ceramic support medium coated with ozone-destroying catalyst is disposed in the housing at the outlet, the porous ceramic support medium having a cell density in the range of 10 to 1000 cells/inch and having a size at least as large as size of the outlet such that the air flow is forced through said porous support medium.
2. A device according to claim 1 wherein the catalyst is manganese dioxide.
3. A device according to claim 1 wherein said porous ceramic support medium is fibrous ceramic.
4. A device according to claim 3 wherein said porous ceramic support medium is fibrous ceramic with cell density in the range 10 to 1000 cells/inch.
5. A device according to claim 4 where the cell density is in the range 50 to 250 cells per inch.
6. A device according to claim 1 wherein said porous ceramic support medium has thickness in the range 0.5 to 2.0 cm.
7. A device according to claim 6 wherein said porous ceramic support medium has thickness in the range 0.7 to 1.3 cm.
8. An electrokinetic air propulsion device, comprising:
a housing having an inlet and an outlet;
a high voltage electrode and a propulsion electrode in said housing, wherein the high voltage electrode and the propulsion electrode are positioned between the inlet and the outlet and wherein the high voltage electrode and the propulsion electrode are configured to be at different potentials to generate air flow in the housing from the inlet to the outlet; and
a porous ceramic medium coated with ozone destroying catalyst, having a cell density in the range 10 to 1000 cells/inch disposed at the outlet, said porous ceramic medium having a size at least as large as size of the housing outlet, such that the air flow from the outlet is forced through said porous ceramic medium.
9. A device according to claim 8 wherein the catalyst is manganese dioxide.
10. A device according to claim 8 wherein said porous ceramic medium is fibrous ceramic.
11. A device according to claim 8 where the cell density is in the range 50 to 250 cells per inch.
12. A device according to claim 8 wherein said porous ceramic medium has thickness in the range 0.5 to 2.0 cm.
13. A device according to claim 12 wherein said porous ceramic medium has thickness in the range 0.7 to 1.3 cm.