Not Applicable
Not Applicable
1. Field of the Invention
This invention pertains generally to for processing pollutant containing gases, and more particularly to nonthermal plasma reactors.
2. Description of Related Art
The emission and discharge of volatile organic compounds (VOCs) are strictly regulated by the U.S. Conservation and Recovery Act (RCRA), the National Pollutant Discharge Elimination System (NPDES), and the National Emissions Standards for Hazardous Air Pollution regulations (NESHAPS). Technical and regulatory difficulties associated with current VOC treatment methods such as air-stripping (dilution), activated-carbon absorption, incineration, and thermal-catalytic treatment have prompted the search for alternatives. The drawbacks of present methods result in ineffective treatment, the generation of large secondary waste streams, and increased costs.
The present invention has recognized the prior art drawbacks, and has provided the below-disclosed solutions to one or more of the prior art deficiencies.
The present invention can be used to effectively treat VOCs while meeting regulations in a timely and economical fashion. In addition to VOCs, the present invention can be used to treat other air pollutants and hazardous/toxic chemicals in gases (e.g., acid rain precursors NOx and SOx, odor causing chemicals, chemical/biological warfare agents, and industrial emissions). Furthermore, to operate fossil-fueled motor vehicles and other combustion-related engines or machinery under higher efficiency and reduced pollution output conditions in the future, it is desirable to have clean-burning, energy-efficient, hydrocarbon liquid fuels. Such higher-order hydrocarbons can be synthesized using a nonthermal plasma (NTP) device according to the present invention.
By way of example, and not of limitation, the present invention is a device that employs electrical discharges/nonthermal plasmas in a gaseous medium to destroy air pollutants or undesirable chemicals/chemical or biological agents, to process chemicals, or to synthesize chemical compounds. In nonthermal plasmas, the electrons are “hot”, while the ions and neutral species are “cold” which results in little waste enthalpy being deposited in a process gas stream. This is in contrast to thermal plasmas, where the electron, ion, and neutral-species energies are in thermal equilibrium (or “hot”) and considerable waste heat is deposited in the process gas.
In the present invention, the NTP reactor is applied to gas streams containing hazardous/toxic, or other undesirable pollutants or contaminants and to gas streams that are to be processed (i.e., changed in chemical form or transformed into other useful products).
In one aspect of the present invention, a nonthermal plasma reactor includes a discharge cell and a charging assembly. The charging assembly provides plural high voltage pulses to the discharge cell. Each high voltage pulse has a rise time between one and ten nanoseconds and a duration between three and twenty nanoseconds.
In another aspect of the present invention, a nonthermal plasma reactor includes a discharge cell and a first charging assembly and a second charging assembly that are electrically connected to the discharge cell. The charging assemblies alternatingly provide opposite polarity high voltage pulses to the reactor.
In yet another aspect of the present invention, a nonthermal plasma reactor includes a first capacitor plate and a second capacitor plate. A dielectric layer is disposed between the first capacitor plate and the second capacitor plate. Further, a spark gap switch is electrically connected to the first capacitor plate and a first electrode is electrically connected to the second capacitor plate. A second electrode is slightly spaced from the first electrode and a dielectric layer is disposed adjacent to the first electrode. Moreover, a gas discharge gap is established between the dielectric layer and the second electrode. In this aspect of the present invention, the first capacitor plate and the second capacitor plate provide plural high voltage pulses to the discharge cell.
In yet still another aspect of the present invention, a nonthermal plasma reactor includes a first capacitor plate, a second capacitor plate, and a first dielectric layer that is disposed therebetween. A first spark gap switch is electrically connected to the first capacitor plate. The reactor further includes a third capacitor plate, a fourth capacitor plate, and a second dielectric layer that is disposed therebetween. Further, a second spark gap switch is electrically connected to the third capacitor plate. In this aspect of the present invention, a first electrode is electrically connected to the second capacitor plate and the fourth capacitor plate and a second electrode is slightly spaced from the first electrode. A dielectric layer is disposed adjacent to the first electrode and a gas discharge gap is established between the dielectric layer and the second electrode. The first capacitor plate, the second capacitor plate, the third capacitor plate, and the fourth capacitor plate alternatingly provide opposite polarity high voltage pulses to the reactor.
In still yet another aspect of the present invention, a nonthermal plasma reactor includes a discharge cell and means for providing plural high voltage pulses to the discharge cell. Each high voltage pulse has a rise time of not more than ten nanoseconds.
In another aspect of the present invention, a method for treating pollutant containing gases includes providing a discharge cell. Plural high voltage pulses are provided to the discharge cell. Each high voltage pulse has a rise time of not more than ten nanoseconds.
In yet another aspect of the present invention, a method for treating pollutant containing gases comprises providing a discharge cell. Plural opposite polarity high voltage pulses are alternatingly provided to the discharge cell. Each opposite polarity high voltage pulse has a rise time of not more than ten nanoseconds.
An object of the invention is to provide a relatively high degree of contaminant removal.
Another object of the invention is to reduce contaminant removal costs.
Another object of the invention is to provide more efficient chemical processing/synthesis.
Another object of the invention is to provide for nonthermal treatment of pollutant containing gases.
Another object of the invention is to provide for simultaneous destruction and removal of multiple pollutants.
Another object of the invention is to eliminate the need for fuels or catalysts.
Another object of the invention is to provide a broad dynamic range for treatment of both rich and lean streams.
Another object of the invention is to provide for higher active species production efficiency with extremely short, high E/N pulses, where E/N is the reduced electric field strength when the process gas experiences electrical breakdown.
Further aspects of the invention will be brought out in the following portions of the specification, wherein the detailed description is for the purpose of fully disclosing preferred embodiments of the invention without placing limitations thereon.
The invention will be more fully understood by reference to the following drawings which are for illustrative purposes only:
Referring more specifically to the drawings, for illustrative purposes the present invention is embodied in the apparatus generally shown in FIG. 1 through FIG. 9. It will be appreciated that the apparatus may vary as to configuration and as to details of the parts, and that the method may vary as to the specific steps and sequence, without departing from the basic concepts as disclosed herein.
Referring initially to
It can be appreciated that a voltage pulse can be applied across the electrodes 10, 12. If the applied voltage pulse rise time and pulse duration are comparable to the streamer transit time across the gap 14, the drive circuit, described below, can influence the development of the discharge across the gap 14. If the applied electric field rises fast enough, each discharge streamer head 20 can coalesce to create quasi-homogenous discharges. It is to be understood that quasi-homogenous discharges can have very favorable consequences. For example, the discharge operates for a larger fraction of its duration at a higher, and more favorable, reduced electric field, i.e., electric field divided by gas density (E/N). Further, the discharge operates at a higher average electron energy.
Further results of the quasi-homogenous discharges are greater yields, i.e., number per unit energy, of free radicals and other active species because these yields generally increase with increasing electron temperature. Moreover, with more homogenous discharges, the radicals are spread over a larger volume and have lower peak concentrations. As such, there is less competition from radical-radical interactions which tend to reduce the concentrations of active species and therefore, more active species survive to react with entrained pollutants or feed gas species.
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Similar to the first charging assembly 204, the second charging assembly 206 includes a first capacitor plate 220 and a second capacitor plate 222. The first capacitor plate 220 rests on a first dielectric layer 224 which insulates it from the housing 202. Also, a second dielectric layer 226 is installed between the capacitor plates 220, 222. A spark gap switch 228 is connected to the first capacitor plate 220.
As shown in
Referring to
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Similar to the first capacitive-transfer circuit 262, the second capacitive-transfer circuit 264 includes a storage capacitor 278 and a peaking capacitor 280 that are connected to the circuit 250 in series to each other and parallel to the electrodes 252, 254.
It is to be understood that the storage capacitors 266, 278 are rapidly switched into the closely coupled peaking capacitors 268, 280. The capacitance of each peaking capacitor 268, 280 is less than its neighboring storage capacitor 266, 278. Accordingly, the peaking capacitors 268, 280 “ring-up” to a higher voltage than the charge voltage on the storage capacitors 266, 278 and electrical discharges are created across the electrodes 252, 254. It is to be understood that in order to deliver very fast time rise pulses to the electrodes 252, 254, the inductances represented by the second inductors 274, 286 in each capacitive-transfer circuit 262, 264 must be kept very low.
It can be appreciated that in each circuit 100, 150, 250 described above additional circuit elements, e.g., resistors, inductors, etc., can be included in order to facilitate pulse shaping.
It is to be understood that each reactor 50, 200 is a fast-pulsed nonthermal plasma (NTP) reactor that can be used to generate highly reactive chemical species, such as free radicals. These reactive species, e.g., O-atoms, OH-radicals, N-radicals, excited N2 and O2 molecules, HO2-radicals, NH-radicals, CH-radicals, etc., readily decompose organic chemicals (e.g., VOCs), oxides of sulfur and nitrogen (SO2 and NOx), and odor agents (e.g., aldehydes, H2S and many others) by breaking their chemical bonds. The result is the production of nonhazardous or easily-managed products. The free radicals, described above, can also play a key role in chemical synthesis, producing desirable products, e.g., creating higher-order hydrocarbon fuels from methane/natural gas.
Further, nonthermal plasmas can be created by the reactors 50, 200. As described in detail above, each reactor 50, 200 makes use of an extremely fast-pulsed dielectric-barrier discharge arrangement. A high voltage pulse having an extremely fast rise time, approximately one to ten nanoseconds (1-10 ns), and duration, approximately three to twenty nanoseconds (3-20 ns), is applied to the electrodes thereby creating electrical-discharge streamers in the gas. With a short enough rise time, the development of the discharges can be influenced such that the discharge gap undergoes electrical breakdown at a reduced electric field, electric field divided by gas density (E/N), much higher than the static field (or the field with a slower rise time)—a condition sometimes called “overvolting”. This can create a quasi-homogeneous discharge condition in which most of the reactor active volume, i.e., the area between the electrodes, is filled with an electrical discharge having a high average electron energy. The discharges are the source of the active nonthermal plasma (NTP).
Each of the above-described NTP reactors 50, 200 are able to reduce hazardous compound concentrations in off-gases to very low levels by free-radical “cold combustion” or synthesize desirable chemical products using gaseous feedstocks. It is to be understood that although each NTP reactor 50, 200, described above, has a generally rectangular box shape, each can be modified to have a generally cylindrical shape.
Although the description above contains many details, these should not be construed as limiting the scope of the invention but as merely providing illustrations of some of the presently preferred embodiments of this invention. Therefore, it will be appreciated that the scope of the present invention fully encompasses other embodiments which may become obvious to those skilled in the art, and that the scope of the present invention is accordingly to be limited by nothing other than the appended claims, in which reference to an element in the singular is not intended to mean “one and only one” unless explicitly so stated, but rather “one or more.” All structural, chemical, and functional equivalents to the elements of the above-described preferred embodiment that are known to those of ordinary skill in the art are expressly incorporated herein by reference and are intended to be encompassed by the present claims. Moreover, it is not necessary for a device or method to address each and every problem sought to be solved by the present invention, for it to be encompassed by the present claims. Furthermore, no element, component, or method step in the present disclosure is intended to be dedicated to the public regardless of whether the element, component, or method step is explicitly recited in the claims. No claim element herein is to be construed under the provisions of 35 U.S.C. 112, sixth paragraph, unless the element is expressly recited using the phrase “means for.”
This invention was made with Government support under Contract No. W-7405-ENG-36, awarded by the Department of Energy. The Government has certain rights in this invention.
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Number | Date | Country | |
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20040182832 A1 | Sep 2004 | US |