The present invention relates to the fields of plasma generation and chemistry.
Currently, the interactions between non-thermal plasma (NTP) and liquid media are mainly utilized in water treatment. Such interactions are usually accomplished by the direct discharge of water and water plasma using various methods. Other approaches involve generating a direct current/alternating current discharge through a water/water vapor interface, or through gas bubbles. These approaches, however, require high voltage pulses, with a corresponding high power consumption, and are limited by their low operating volumes.
A non-thermal plasma (NTP)-liquid interface is generated using a gas-buffered housing having a gas inlet and nozzle, and a gas discharge plasma reactor. Gas is made to flow through or around the gas discharge plasma volume so as to create a gas pressure inside the housing that is greater than the overall pressure at exit of the nozzle, including the pressure due to depth of the liquid media and the pressure above the liquid. Under such conditions, the plasma inside the housing is sustained and the plasma activated species (PAS) is injected directly into the liquid via the nozzle. The chemical reaction of PAS with liquid effectively occurs at the surface of the gas cavity around the nozzle and on the surfaces of micro-liquid droplets that exist within the gas cavity.
The present invention provides a simple and convenient NTP-liquid interface system for the direct injection of PAS into liquid, thus improving the overall efficiency of the plasma-liquid interaction. The invention has a simple construction, is compact and can be operated in a safe, clean and scalable way.
When the gas outlet 22 is submerged into the liquid 14, gas should be provided at the inlet 20 so as to maintain the pressure in the housing 12 equal to or higher than the overall pressure (pressure from the liquid solution 14 above the gas outlet 22 and the pressure above the liquid 14) at the gas outlet 22, so that liquid 14 does not flood the housing 12 through the gas outlet 22 and the discharge plasma 28 in the housing 12 is sustained. The housing 12 expels gas as a mixture of inflow gas and PAS. The PAS interacts with the liquid 14 on the surfaces of gas bubbles 32 expelled from the gas outlet 22. Moreover, micro-liquid droplets 34 that exist in the gas bubbles 32 and, especially, the gas-liquid interface 36 at the quasi-steady gas cavity 38 formed at the gas outlet 22 cause a tremendous increase of the surface area available for chemical reactions, leading to a much higher efficiency of conversion of the chemical species in the liquid 14.
The cup-like housing 44, whether grounded or electrically biased, acts as the gas-buffered housing, which will also be referenced herein by the numeral 44. A NTP discharge plasma 54 is generated separately in a plasma reactor (not shown) and enclosed in the gas-buffered housing 44. Any electrically-isolated cup-like structure within or outside of the MHCD may perform as a gas-buffered housing 44, as long as it is electrically isolated from the plasma reactor and allows gas flow to exit through the gas outlet 50. The gas-buffered housing 44 may be integral to the plasma reactor. Gas plasma flow f2 into the housing 44 can be maintained through the gas inlet 48.
For a series of experiments, a NTP-liquid interface system was constructed with a gas-buffered housing 44 integrated with a plasma reactor. A DC micro-discharge plasma 54 was generated using the MHCD 40 having a metal-dielectric-metal structure with a millimeter-size hole penetrating all of the structural layers. The thickness of the dielectric layer 46 was controlled to be less than 1 mm so that the dielectric 46 would readily break down at high gas pressures. The electrically-grounded gas-buffered housing 44 was integrated with the anode of the plasma reactor, so that the gas discharge plasma 54 would be placed at the gas outlet 50 of the housing 44.
Various gasses (air, O2, N2, Ar, Ne, He, and mixtures of such gasses) were used as the working gas and the gas flowing through housing 44. The PAS was carried by the gas and directly injected into a liquid (such as tap water, de-ionized water, bio-enriched water, methanol, oil, etc.) through gas outlet 50. When operated in ambient air, the clear plasma plume 56 (i.e., afterglow) was present which showed very little change when the gas outlet 50 was submerged into liquid.
The arrangement of the electrical circuit allowed almost 80% of the power from the power supply 52 to dissipate on the plasma discharge, improving the overall efficiency of the process. The voltage within the flow of PAS and electromagnetic radiation at the gas outlet 50 was measured to be up to 25 V with respect to electrical ground. A negative ion current of 1 mA to 1 nA was detected at distances ranging from 0.1 cm up to 20 cm from the gas outlet 50.
When air was used as working gas, direct oxidation of water was achieved in an extremely efficient way without discharging the water itself through the gas outlet 50. The hydrogen peroxide (H2O2) production rate was at least three times better from the best existing plasma-solution interaction method known to the inventors (i.e., capillary discharge in water, as discussed in Nikiforov; A. Yu., and Leys, C, “Influence of capillary geometry and applied voltage on hydrogen peroxide and OH radical formation in AC underwater electrical discharges”, Piasma Sources Sci. Technol. 16 (2007) 273-280, the disclosure of which is incorporated herein by reference).
The gas flow rate into the gas-buffered housing 44 is closely related to the diameter “a” and depth “b” of the gas outlet 50, the pressure above the liquid 14 and the depth to which the gas outlet 50 is submerged. The effectiveness of the injection of PAS into liquid depends on the diameter “a” and depth “b” of the gas outlet 50, the distance from the plasma reactor to the gas outlet 50, and the flow rate of the gas into the liquid 14.
A combination of two NTP-liquid interface systems may be opposed to each other with one gas-buffered housing biased positively to serve as a virtual anode and the other biased negatively to serve as a virtual cathode. With a flow of gasses from both systems, a gas discharge may be sustained within a quasi-steady state gas cavity generated between the opposing gas outlets.
Although the invention has been described and illustrated in detail, the following, non-limiting, experimental example may be useful to further illustrate application of the invention.
PAS generation: PAS was generated via a MHCD structure, similar to that shown in
Introducing PAS into de-ionized water: The apparatus described above was set to create PAS continuously. As the apparatus was held stationary in a vertical position, a beaker containing 100 ml of de-ionized water was raised towards the gas outlet 50 of the gas-buffered housing 44 through a z-stage until the outer surface of the gas outlet 50 was about 2 cm below the surface of the de-ionized water. The flow of ambient air was controlled at a constant rate of about 30 ml/s and allowed to bubble out of the gas outlet 50. The PAS was introduced into the water continuously for about 15 minutes.
Measurement of the H2O2 concentration: The concentration of H2O2 in the treated water sample was evaluated using a HACH® hydrogen peroxide test kit (Model HYP-1; HACH Company, Loveland, Colo., USA). Ammonium molybdate solution was added to the treated de-ionized water sample, followed by the addition of HACH® Sulfite 1 reagent powder. After mixing, the color of the sample turned into a dark blue that was almost black. After 5 minutes, about 1 ml of the prepared sample was collected, and sodium thiosulfate titrant was added drop by drop until the color disappeared completely. Each drop of sodium thiosulfate titrant was counted as 1 mg/L of H2O2.
The H2O2 test showed that about 80 mg of H2O2/L of de-ionized water was produced during 15 minutes of direct introduction of PAS. This amount of H2O2 produced in similar tests would be dependent on air flow rate and electrical current.
pH test: The pH of the treated de-ionized water was tested using a standard pH paper test strip. No obvious color change is observed in tests made on the treated sample, indicating that there was no discernable deviation from the initial liquid pH of 7.
Ion current measurement outside of the gas outlet: The apparatus described above was held vertically, with ambient air as the working gas. Air flow and electrical current were maintained at about 30 ml/s and about 20 mA, respectively. An aluminum plate was connected to an ammeter to detect the ion current outside of the gas outlet 50. The distance of the surface of the aluminum plate from the outer surface of the gas outlet 50 was varied from 0.1 cm to 20 cm. The detected negative ion current was observed to decay with increased distance and ranged from 1 mA at a distance of 0.1 cm to 1 nA at 20 cm.
It should be understood that the embodiments described herein are merely exemplary and that a person skilled in the art may make many variations and modifications thereto without departing from the spirit and scope of the present invention. All such variations, and modifications, including those discussed above, are intended to be included within the scope of the invention, which is described, in part, in the claim presented below.
This application claims benefit of U.S. Provisional Patent Application No. 60/969,326, filed Aug. 31, 2007, and U.S. Provisional Patent Application No. 61/128,675, filed May 23, 2008, the disclosures of which are incorporated herein by reference.
Number | Date | Country | |
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60969326 | Aug 2007 | US | |
61128675 | May 2008 | US |