Patent Application
20230356174
The invention relates to devices for disposal of waste in solid, liquid and gaseous state thereof, in particular, it relates to devices for providing waste disposal by plasma-chemical destruction.
There is a known method of conversion of solid organic waste according to patent RU 2741004 (published on 22 Jan. 2021), wherein conversion of solid organic waste is performed by way of steam plasma gasification with obtaining syngas. The treatment is provided using a high-temperature plasma reactor that employs water steam as a plasma forming gas and provides a temperature of about 1600-2000° C. in the active area.
Limitations of this reactor are incomplete conversion of solid organic waste since the result of conversion is syngas that shall also be converted, and its inability to convert non-organic substances of residential solid waste.
A technical effect obtained by this invention is implementation of a reactor providing destruction of both organic and inorganic substances of residential solid and/or liquid waste.
The technical effect is obtained with a reactor provided in form of a closed cavity having an input orifice connected to a waste feed apparatus and an output orifice for outputting gaseous products of destruction. Inner surfaces of the cavity are made electrically conductive entirely or partially and an electrode is inserted into the reactor, wherein the electrode is isolated from the conductive surfaces and connected to a source of high-voltage pulses and size of a gap between the electrode and the conductive surfaces of the cavity provides formation of plasma streamers of corona discharge.
Preferably, the electrode is cylindrically shaped and has a sharpened tip.
Preferably, the electrode is made of steel.
In one embodiment, the cavity bottom is covered with a conductive moisture-contained liquid.
Preferably, the gap between the electrode and at least one portion of the inner conductive surfaces of the cavity or surface of the conductive moisture-contained liquid covering such a portion is provided in range of 5 to 50 mm.
Preferably, the conductive portions of the inner surfaces of the cavity are made of steel or other metal and grounded.
In one embodiment, inner non-conductive surfaces of the cavity may have a protective coating made of a dielectric material.
In one embodiment, the cylindrical electrode is equipped with ribs provided in form of steel strips attached to the electrode by short sides thereof, while long sides of the steel strips are directed to the electrode and the ribs are angularly disposed relative to the electrode towards the sharpened tip of the electrode.
Preferably, the angle between the steel strips and the electrode axis is selected in range of 20 to 60 degrees. Preferably, 3 to 6 steel strips are to be used.
In one embodiment, the cavity bottom is flat and conductive and the cylindrical electrode is located transversally to the bottom with a gap.
In one embodiment, a steel grid is secured in parallel to the bottom through isolating spacers attached to the bottom. The grid has an opening for the cylindrical electrode so as a gap is formed around the electrode and free ends of the ribs abut on the isolating spacers secured to the grid.
Preferably, the gap around the cylindrical electrode is provided in range of 3 to 10 mm, but it is less than the gap between the cylindrical electrode tip and the conductive bottom. Preferably, pressure inside the reactor is lower than atmospheric pressure by 0.1 to 1 Pa.
In one embodiment, the under-pressure inside the reactor is provided by connecting an electrostatic filter with a sucking air blower to the output orifice. Preferably, the reactor is implemented with limitation of intake of air. In one embodiment, the limitation of intake of air is provided by use of a wad that closes the reactor inlet, wherein the wad is pre-formed by pressurizing waste prior to feeding to the reactor.
It is to be understood that both the foregoing general description and the following detailed description are exemplary and explanatory and are intended to provide further explanation of the invention as claimed.
The accompanying drawings, which are included to provide a further understanding of the invention and are incorporated in and constitute a part of this specification, illustrate embodiments of the invention and together with the description serve to explain the principles of the invention.
In the drawings:
Reference will now be made in detail to the preferred embodiments of the present invention, examples of which are illustrated in the accompanying drawings.
1—reactor body with inner cavity;
2—input opening;
3—output opening;
4—inner surface of reactor cavity;
5—conductive portions of inner surface of reactor cavity;
6—tipped electrode;
7—isolating members;
8—source of high-voltage pulses;
9—electrode tip;
10—conductive bottom of reactor;
11—device for dosed loading waste to be treated;
12—electrostatic filter with extraction air fan providing depression at reactor output.
The invention may be implemented in a reactor having a body. The reactor body has an input orifice 2 connected to an apparatus 11 for metered feed of solid and/or liquid waste to be processed. The apparatus 11 is configured to limit amount of air that is let into the reactor. The reactor body has an output orifice 3 intended for removing gaseous destruction products and connected to an electrostatic filter with a sucking air blower. Portions 5 of the body cavity inner surface and a bottom 10 are made of steel. An electrode 6 is inserted into the cavity of the body 1 through an isolating spacer 7. The electrode 6 is connected to a source 8 of high-voltage pulses. A tip 9 of the electrode 6 is located with a gap of 20 mm relative to the conductive bottom 10 of the reactor body 1.
The device is operated in the following way. High-voltage pulses are fed to the electrode 6 from the source 8. As known from [1], each pulse causes a large number of streamers in the neighborhood of the tip 9 of the electrode 6. The streamers multiply and spread towards the conductive bottom 10 of the body 1, gradually populating the inter-electrode gap and forming corona discharge. After that, for example, a portion of pressed solid residential waste is fed into the device from the apparatus 11 for metered feed of waste to be processed via the input orifice 2, so intake of atmospheric air into the body 1 via the input orifice 2 is limited. Corona discharge plasma acts on water contained in input waste causing generation of free radicals upon disruption of water molecule H2O→OH⋅+H⋅. Additionally, streamers of pulse corona discharge cause formation of other active substances, namely O3, O2(a1Δ), H2O2, OH, O(3P), NO, HNO2 and HNO3 in the reactor. Corona discharge is also a source of ultraviolet (UV) radiation. The active substances and UV radiation provide a disruptive impact upon any organic and inorganic substances contained in waste to be processed, thus assuring disintegration thereof with formation of harmless gaseous products, namely water and carbon dioxide. Inorganic content of waste is disrupted by acids HNO2 and HNO3 formed in the reactor due to the corona discharge. Oxidation process in water for organic substances is a chain reaction [2]. A low rate chain reaction may be initiated by atmospheric oxygen and ozone. A high rate chain reaction is initiated by OH⋅ radicals. In other words, plasma-chemical destruction of both organic and inorganic substances contained in waste is provided in the device. Gaseous destruction products flow into the output orifice of the reactor.
Thus, the indicated technical effect is obtained by the device owing to plasma-chemical destruction of both organic and inorganic substances contained in residential waste.
Having thus described a preferred embodiment, it should be apparent to those skilled in the art that certain advantages of the described method and apparatus have been achieved.
It should also be appreciated that various modifications, adaptations, and alternative embodiments thereof may be made within the scope and spirit of the present invention. The invention is further defined by the following claims.
[1] Aristova N. A., Piskarev I. M., Ivanovskiy A. V., Selemir V. D., Spirov G. M., Shlepkin S. I., Initiation of chemical reactions by electrical discharge in dielectric-gas-liquid configuration. // Physical Chemistry Journal, 2004, Vol. 78, #7, pages 1326-1331.)
[2] Piskarev I. M., Oxidation-reduction processes in water initiated by electrical discharge above water surface. //General Chemistry Journal, 2001, Vol. 71, Issue 10, page 1622.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2021140063 | Dec 2021 | RU | national |
| Number | Date | Country | |
|---|---|---|---|
| Parent | PCT/IB2022/058935 | Sep 2022 | US |
| Child | 18221733 | US |
