Patent Grant
8308846
The present disclosure relates to a method for precipitating liquid and/or particle-shaped impurities from a stream of gas, for example, for precipitating oil droplets, soot particles, and/or dust from a stream of blow-by gas that originates from a crankcase of an internal combustion engine and is directed to the intake side of the internal combustion engine. In this context, the stream of gas that is to be cleaned is passed through a gas discharge section between at least two electrodes, of which at least one electrode is an active or emission electrode (cathode) and at least one other electrode is a precipitation or counter-electrode (anode), by means of which the impurities to be precipitated from the stream of gas are electrically charged and sucked in or attracted by the counter-electrode by means of electrical field forces.
The present disclosure further relates to a device for precipitating liquid and/or particle-shaped impurities from a stream of gas, for example, for precipitating oil droplets, soot particles, and/or dust from a stream of blow-by gas that originates from the crankcase of an internal combustion engine and is directed to the intake side of the internal combustion engine. The device includes at least two electrodes that are set apart from each other and between which the flow path of the gas stream runs. One of the electrodes is an active or emission electrode (cathode) and the other electrode is a precipitation or counter-electrode (anode), by means of which the impurities present in the stream of gas can be electrically charged and can be sucked in or attracted by the counter-electrode by means of electrical field forces.
A comparable method and a comparable device for cleaning crankcase ventilation gases are known from MTZ Motortechnische Zeitschrift 60 (1999) 7/8. In this case, there is a central wire electrode that is operated with a voltage below the breakdown voltage and which is encircled at a distance by a coaxial counter-electrode as the anode, so that the gas stream to be cleaned can flow through this tubular counter-electrode.
In view of the flow rate of the gas to be cleaned, this device is not suitable for effective cleaning because of its limited length. In addition, there is a considerable risk of fouling the wire electrode, which may result in the device operating in a non-homogeneous way and thus ineffectively.
In addition, particle separators, which precipitate charged particles from a gas stream at a flat electrode by means of electrical field forces, exist in a variety of embodiments, for example, as an electrostatic dust filter or as a so-called oil separator for cleaning crankcase ventilation gases. These embodiments all share a common feature that the electrical field is generated with as high an electrical field strength as possible, although the electrical voltages have to be significantly below the breakdown voltage for the electrode gap of such electronically operated separators. Usually, the operating voltage is less than half the breakdown voltage, in order to avoid uncontrolled local discharges (electrical voltage breakdown).
The result is low efficiency and a long path is required for the actual separation, especially if the flow rate of the gas conveying the particles is high.
In addition, large scale treatments of exhaust gas for clean air can be carried out with plasma technology. In this case, a plasma technology with pulsed electric filters is used, where the pulse exhibits peak power of 50 megawatts at pulse rates of 200 hertz. The plasmas in these particle filters are superposed with high voltage pulses. Such a device is expedient only in connection with large scale industrial plants.
Therefore, an object is to provide a method and a device of the genre described in the introductory part, with which effective cleaning of a gas stream is possible even under restricted space conditions, even if this gas stream exhibits a high flow rate.
For achieving this object, a gas stream is passed between at least one electrode tip, which serves as an emission electrode (cathode), and a counter-electrode (anode), which is positioned at a distance from said emission electrode. A direct voltage, exceeding the breakdown voltage, is applied to the electrodes. The current of the gas discharge section that establishes itself between the two electrodes is limited, by means of which a stable low energy plasma is formed in the space between the two electrodes.
In this way, a direct current plasma of the “non-equilibrium plasma under atmospheric pressure” type can be generated between the electrodes in the gas stream or flow channel of the gas to be cleaned. The result is a direct current plasma having a high electron density, but a comparatively low temperature, so that gas that is directed through this plasma, and in particular its impurities, very quickly assume a high charge and can be attracted correspondingly fast by the counter-electrode so that, given a low space requirement, an effective precipitation of the impurities from a gas stream is possible, even if this gas stream exhibits a high flow rate.
Owing to the negative current-voltage characteristic of such a plasma, the current that establishes itself between the electrodes is limited. The present disclosure makes use of the fact that in the case of such a direct current plasma, the ions and the neutral gas particles exhibit a significantly lower temperature of, for example, less than 100° C., and that the number of negative electrons and the number of positive gas ions of the gas bearing the impurities to be precipitated are not in a state of equilibrium.
In this case, it is practical to apply to the electrodes a voltage that is at least 1.2 times or one and one-half times the breakdown voltage. Therefore, in order to generate the direct current plasma, a high electric voltage, which significantly exceeds the breakdown voltage, is used. A non-equilibrium plasma of high electron density is generated in the space between the electrodes. In this space, even large particles to be precipitated can be electrically charged to the maximum degree, in order to precipitate at the counter-electrode by the shortest route.
The limited current between the electrodes can expediently be selected in proportion to the flow rate and can be increased at a higher flow rate, a feature that results in the highest possible efficiency, so that the implementation of the method has a space requirement that is kept as low as possible.
The method becomes especially effective and efficient if the gas stream is directed past a plurality of electrode tips, which form the active (or the emission) electrode. In the event that the active electrode exhibits an adequately high density of electrode tips, the limit charge of the polluting particles in the gas stream can be reached as a function of the configuration of these tips. In particular, with the use of a tip array as the active electrode, a very effective cleaning can be achieved by the shortest route, thus, in a space saving manner, even if the gas to be cleaned exhibits a high flow rate.
The present disclosure provides a device with which, even under restricted space conditions, an effective cleaning of a gas stream is possible, even if this gas stream exhibits a high flow rate. For example, a device of the type described in the introductory part may be provided in which the precipitation electrode or counter-electrode (anode) is provided in a flat form and is combined with an active electrode (cathode) that is positioned at a distance from said counter-electrode and which exhibits at least one tip that is aimed in the direction of the flat electrode. In order to limit the current, a current limiting element is provided on the current supply path to this tip that forms the active electrode.
With such a device, it is possible to generate an equilibrium plasma having an electron density of about 1010 electrons per cubic centimeter and electron temperatures of up to 50,000° C. between the electrodes in the flow channel of the gas to be cleaned. However, at the same time, the ions and the neutral gas particles exhibit a significantly lower temperature of less than 100° C. and the number of negative electrons and the number of positive gas ions of the gas bearing the particles to be precipitated are not in a state of equilibrium. In this way, an effective precipitation of impurities at the flat electrode can be achieved by a relatively short route.
The current limiting element at the active electrode designed as a tip can be a resistor or a semiconductor. This approach constitutes a simple arrangement of high effectiveness.
It is especially advantageous if the active electrode or the emission electrode (cathode) is formed by a plurality of tips. Correspondingly large is the field volume, in which the direct current plasma is formed, so that the particles to be precipitated are charged by the shortest route and can precipitate at the flat counter-electrode.
In one embodiment of the device according to the invention, the tips forming the emission electrode (cathode) are arranged in several rows, which are situated one after the other in the direction of flow of the gas to be cleaned. The tips of each row are offset, preferably laterally, in relation to the tips of the next row. As a result, there is an overlapping of the direct current plasma in the direction of flow, a state that in turn results in the space between the electrodes being practically filled with this direct current plasma, thus preventing any gaps from remaining open in the direction of flow.
Therefore, the emission electrode can be designed expediently as an emission tip array and can appear as a grid, which eliminates gaps in the plasma formed between the electrodes for a selected flow cross section of the gas stream in the direction of motion of the particles. The respective next row of tips is arranged so as to be offset by a fraction of the basic grid width. When there is an adequate number of such rows of tips that are arranged one after the other in the direction of flow, the result is a desired closed plasma arrangement in the direction of flow so that the targeted cleaning can take place by a relatively short route even in the case of a high flow rate.
It is advantageous if, in at least one embodiment of the device according to the invention, in use, a direct voltage that is higher than the breakdown voltage is applied between the electrodes and, if a device for current limiting is provided at the active electrode(s).
In this way, it is possible to attach each of the tips of the emission electrode by means of a plasma current limiting element, for example, a high impedance resistor, to a preferably negative direct current high voltage source of which the operating voltage exceeds the breakdown voltage to the conductive counter-electrode, which is configured in a flat form opposite the tip array. As a result, a non-equilibrium plasma having an electron density of about 1010 cm−3 is generated in the space between each tip of the tip array and the flat counter-electrode connected to the positive pole of the direct voltage source, in which space also the largest particles to be precipitated are electrically charged to the maximum amount and precipitate on the opposite flat counter-electrode by the shortest route.
At the same time, it is advantageous for precipitating the impurities as uniformly and effectively as possible, if the tips forming the active electrode are arranged in a plane and if the counter-electrode is designed so as to be planar and flat and is arranged parallel to the plane, in which the tips of the active electrode are arranged. In this way, all of the tips of the active electrode exhibit identical spacing, with virtually constant conditions regarding the direct current plasma that is formed resulting in the whole device.
The device may include a housing on the floor of which the counter-electrode lies flat, and, at a distance thereto, tips forming the active electrode can be provided between side walls of the housing. The housing has an inlet and an outlet for the gas stream. This constitutes an arrangement that is especially practical from a design point of view for arranging and housing the electrodes in a practical way and to pass the gas stream between them.
In another practical embodiment of the invention for even better precipitation or cleaning results, the device includes a mechanical separator, in particular, for relatively large droplets or particles, upstream of the electrodes in the direction of flow. Thus, prior to the precipitation between the electrodes, larger particles can already be precipitated mechanically so that they no longer strain the electronic precipitation. With this arrangement, the entire system can operate with correspondingly less electrical energy. This approach may above all be advantageous in non-stationary systems, for example, in the engines of vehicles.
For example, it is possible that the mechanical separator be designed as an impingement separator with at least one baffle or that said mechanical separator is a cyclone separator. Such mechanical separators are known per se and can be selected and adapted in a practical way for the intended application.
An aperture or bore for a return of precipitated oil or for removing the precipitated particles can be provided between the mechanical separator and the electrode separator. As a result, if cleaning is necessary, it may be done at longer time intervals than if the precipitated oil droplets and particles were to be evacuated only by means of cleaning processes.
An additional embodiment of the device, according to the invention, can provide that emission electrodes designed as tips are arranged on both sides of a flat or plate-shaped counter-electrode. In this way, an effective precipitation of impurities or particles from a gas stream can be achieved in an even narrower space.
Since the polluting particles can assume a high charge, both such a configuration with emission electrodes arranged on both sides of a plate-shaped counter-electrode and also a configuration with emission electrodes designed as tips on just one side of a flat plate-shaped counter-electrode, can be carried out in such a space-saving way that the entire device can be incorporated or installed, for example, into the cylinder head covers or intake pipes of internal combustion engines or also into other modules and components that are in communication with a stream of gas that is to be cleaned.
In particular, when individual or multiple features and measures described above are combined, the result is a method and a device for precipitating impurities from a stream of gas with which the avoidance of uncontrolled local discharges does not have to be at the expense of poor efficiency and a very long path length for the actual precipitation, but rather a high efficiency can be achieved by means of a direct current plasma of the “non-equilibrium plasma under atmospheric pressure” type, even if very little space in the direction of flow is available. In this context, the flow channel can have preferably a rectangular cross section, wherein this rectangular cross section can be defined by the two electrodes on two opposite sides.
Embodiments of the invention are described in detail below with reference to the drawings in which
In the following description of the embodiments, those parts that exhibit identical functions have identical reference numerals, even if the shape of these parts is somewhat different.
A device, which is labeled with the reference numeral 1 in all three figures, serves for precipitating liquid and/or particle-shaped impurities from a stream of gas, which is indicated by the arrow Pf in
To this end, the device 1 exhibits two electrodes which are spaced apart from each other, in all of the embodiments between which the flow path of the gas stream Pf runs, wherein one of the electrodes is an active or emission electrode 2 or cathode and the other electrode is a precipitation or counter-electrode 3 or anode with which the impurities in the stream of gas Pf can be electrically charged and can be sucked in or attracted by the counter-electrode 3 by means of electrical field forces.
Furthermore, it is clear in all three figures that the precipitation electrode or counter-electrode 3 is designed so as to be flat and plate-shaped and planar, and that this counter-electrode 3 is combined with a spaced-apart active or emission electrode 2, which is formed by a plurality of tips 4 that are aimed at the flat electrode 3 and are arranged in a common plane, which runs parallel to the counter-electrode 3 at a distance from it so that the flow path for the gas stream Pf between these electrodes 2 and 3 is limited on two sides.
In this case,
In particular, when all three figures are viewed simultaneously, it becomes clear that the tips 4 forming the emission electrode 2 or cathode can be arranged in multiple rows located one after the other in the direction of flow, wherein the tips 4 of one row are offset laterally in relation to the tips of the next row.
The aforesaid applies all the more to the arrangement in
In
Thus, in all of the embodiments depicted in the figures, the emission electrode 2 is designed as an emission tip array and appears as a grid. For a selected flow cross section, the emission tip array has a rectangular cross section in the embodiments. This prevents gaps in the plasma 7 formed between the electrodes 2 and 3 for the gas stream in the direction of motion of the particles by means of the above described overlapping of the plasma cones, because the respective next row of tips 4 is arranged so as to be offset by a fraction of the basic grid width.
In all three embodiments the device 1 has a housing 8, on the floor 9 of which the counter-electrode 3 lies flat on the inside. Positioned at a distance from said counter-electrode 3, the tips 4 forming the active electrode 2 are provided between the side walls 10 of this housing 8. The housing 8 has an inlet 11 and an outlet 12 for the stream of gas Pf. The inlet 11 and the outlet 12 are not shown in
Between the mechanical separator 13 and the electrode separator, respectively, the inlet 11, one can see a downwardly directed aperture 18 or bore, which can serve as the return of the mechanically precipitated oil.
With the above described device 1, according to
| Number | Date | Country | Kind |
|---|---|---|---|
| 10 2007 025 416 | May 2007 | DE | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/EP2008/003798 | 5/10/2008 | WO | 00 | 6/3/2010 |
| Publishing Document | Publishing Date | Country | Kind |
|---|---|---|---|
| WO2008/145251 | 12/4/2008 | WO | A |
| Number | Name | Date | Kind |
|---|---|---|---|
| 2195431 | Shively et al. | Apr 1940 | A |
| 3648437 | Bridges | Mar 1972 | A |
| 4138233 | Masuda | Feb 1979 | A |
| 4152124 | Davis | May 1979 | A |
| 5476539 | Suzuki et al. | Dec 1995 | A |
| 6186128 | Diotte | Feb 2001 | B1 |
| 7267711 | Liu | Sep 2007 | B2 |
| 7547353 | Reyes et al. | Jun 2009 | B2 |
| 7601205 | Furukawa et al. | Oct 2009 | B2 |
| 7651553 | Pletcher et al. | Jan 2010 | B2 |
| 7753994 | Motegi et al. | Jul 2010 | B2 |
| 7785404 | Leng et al. | Aug 2010 | B2 |
| 20060278082 | Tomimatsu et al. | Dec 2006 | A1 |
| 20080202331 | Abdelkrim et al. | Aug 2008 | A1 |
| Number | Date | Country |
|---|---|---|
| 1 277 928 | Jan 2003 | EP |
| 1 451 222 | Sep 1976 | GB |
| 5-154409 | Jun 1993 | JP |
| 9925972 | May 1999 | WO |
| 0069537 | Nov 2000 | WO |
| 0192694 | Dec 2001 | WO |
| 2005049215 | Jun 2005 | WO |
| 2005119020 | Dec 2005 | WO |
| 2006128711 | Dec 2006 | WO |
| Number | Date | Country | |
|---|---|---|---|
| 20100294129 A1 | Nov 2010 | US |
