EP2062649A2 - Electrostatic separator with particulate rejection means, heating system and method for operation - Google Patents
Electrostatic separator with particulate rejection means, heating system and method for operation Download PDFInfo
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- EP2062649A2 EP2062649A2 EP08019567A EP08019567A EP2062649A2 EP 2062649 A2 EP2062649 A2 EP 2062649A2 EP 08019567 A EP08019567 A EP 08019567A EP 08019567 A EP08019567 A EP 08019567A EP 2062649 A2 EP2062649 A2 EP 2062649A2
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- electrode
- particles
- exhaust gas
- channel
- flow direction
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/34—Constructional details or accessories or operation thereof
- B03C3/88—Cleaning-out collected particles
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/34—Constructional details or accessories or operation thereof
- B03C3/74—Cleaning the electrodes
Definitions
- the invention relates to an electrostatic precipitator, in particular for an exhaust pipe of an exhaust gas purification system, according to the preamble of claim 1. Furthermore, the invention relates to a heating system for generating energy by burning an energy source with an electrostatic precipitator according to the preamble of claim 7. In addition concerns the invention a method for reducing deposits of particles of an exhaust gas flow to an electric field generating electrode of an electrostatic precipitator of a heating system according to the preamble of patent claim 8.
- the GB 2 045 647 A describes an electrode of an ionization device for an electrostatic air filter.
- the electrode comprises a current-conducting wire which is clamped in a frame in a plurality of mutually parallel, electrically connected series sections.
- the electrode also includes glands, sleeves and springs.
- the wire is hung in the anchor bolt, passed freely through the space formed by the frame, threaded through the fitting, the hose-like protective sleeve and the screw, again guided through the free space, etc. Finally, the wire ends in the compression fitting with which the wire can be stretched.
- the JP 2007 263 754 A describes a cleaning device for an electrode of an emission spectrometer.
- the cleaning device comprises a brush with a metal wire brush attachment.
- the brush is functionally and constructively separated from the electrode and is used outside of the meter operating times. In a pause between two measuring operations, the cleaning device brushes over the electrode and removes scraping residues of condensed metal vapor.
- An emission control system which is used for biomass heating systems to reduce particulate matter emission.
- the device described therein can be installed in a flue gas channel and for this purpose has a lid which can be placed gas-tight on an associated opening on a flue gas channel.
- a spray electrode for example in the form of a tensioned rod, is held over an insulating holder.
- a high-voltage transformer with rectifier function allows the construction of a high DC voltage between the wire and the lid, which is electrically connected to the furnace tube, so that it acts as a collector electrode.
- Such an electrostatic filter with a spray electrode and a collector electrode is also known as an electrostatic precipitator.
- This is used for exhaust gas purification in an exhaust pipe of a heating system.
- a capacitor is formed by the spray, which runs approximately centrally through the exhaust pipe and therefore also referred to as the center electrode, and a peripheral surface of the exhaust pipe, which is also referred to as a cylindrical capacitor in a cylindrical tube-shaped design of the exhaust pipe.
- the spray or center electrode generally has a circular cross section in the flow direction of the exhaust gas, wherein the diameter of the cross section or the radius of curvature is generally formed relatively small (for example, less than 0.4 mm).
- a field extending transversely to the flow direction is formed by field lines from the center electrode to the collector electrode through the center electrode and the collector electrode formed by the lateral surface.
- a high voltage is applied to the center electrode, for example in the range of 15 kV.
- a corona discharge is formed, through which the particles flowing through the field in the exhaust gas are charged in a unipolar manner. Due to this charge, most of the particles migrate through the electrostatic Coulomb forces to the inner wall of the exhaust pipe, which serves as a collector electrode.
- the particles are electrostatically charged by the corona discharge which forms along the surface of the electrode. This happens At the molecular level, by the following process: If, for example, the electrode is at a negative high voltage relative to the exhaust pipe, a large number of gas molecules will be negatively charged. They move in the electric field applied by the electrode and the exhaust pipe in the direction of the exhaust pipe. If these meet on their way through the exhaust pipe to electrically neutral particles, they stick to these and charge the previously neutral particles also negative. The charged particles flow driven by electrostatic deflection forces to the inner wall of the exhaust pipe. Here the particles stick, lose their charge and are safely removed from the exhaust stream.
- Burning produces bipolar charged particles.
- the distribution is symmetrical, ie there are the same number of positive and negatively charged particles.
- the number of charged particles is reduced by approx. 10% per second due to coagulation, there are still more than 10% charged particles at the electrostatic precipitator (corresponding to about one to two seconds of particle flying time from the place of combustion).
- the electrostatic precipitator corresponding to about one to two seconds of particle flying time from the place of combustion.
- a disadvantage of the electrostatic precipitators according to the prior art is that it comes after a longer period of operation to a continuous degradation of the corona current at a constant high voltage. As a result, the charging efficiency of the electrode decreases, which in turn reduces the separation efficiency of the entire system.
- the invention has for its object to provide an electrostatic precipitator, which overcomes this disadvantage and in particular prevents or reduces the deposition of particles on the electrode to increase the service life of the electrostatic precipitator.
- the invention has for its object to provide a heating system with a separator according to the invention, which guarantees reliable exhaust gas purification.
- the invention has for its object to provide a method according to which the permanent deposition of particles on the electrode is prevented or at least reduced.
- the electrostatic precipitator according to the invention is characterized in that in the electrostatic precipitator, in particular for an exhaust pipe of an exhaust gas purification system, with a flow channel having a channel wall and a channel inside, through which a particle-containing exhaust gas flows in a flow direction, and in the channel interior substantially in Provided flow direction extending electrode, for forming an electric field between the electrode and the channel wall, is provided that further comprises a Pumbleabweisesch is included, which prevents particles of the exhaust gas to deposit on the electrode.
- the particle repelling agent effectively prevents or reduces the deposition of particles on the electrode.
- the particle-repelling means comprises at least one pre-electrode unit, which is arranged in front of the electrode in the flow direction of the exhaust gas in order to form an electric field in the flow direction in front of the electrode.
- the pre-electrode unit is designed such that it uses a voltage level which is the same as the electrode. On the Vorelektrodeniser but also a different voltage level to the electrode may be applied, which is higher or lower than that of the electrode. This realizes an effective filter function.
- the pre-electrode unit has a pre-electrode which has the same polarity as the electrode. In this way, it is ensured that particles which would reach the electrode without a pre-electrode unit reach the pre-electrode at the upstream pre-electrode unit.
- the pre-electrode thus acts as a kind of "sacrificial electrode".
- An embodiment provides that the pre-electrode is formed as conductively connected to the electrode. This ensures that the electrode and the pre-electrode have the same polarity.
- the pre-electrode is formed differently from the electrode.
- the pre-electrode is formed differently from the electrode, in particular with regard to the parameters required for generating an electric field. The differences may be in geometry, material, manufacturing method, surface structure, and the like.
- the pre-electrode is formed in one preferred embodiment in one piece with the electrode.
- the pre-electrode is formed with respect to the electrode as a thickening.
- An embodiment of the invention provides that at least one of the electrodes is at least partially formed as a tuft-like arrangement of wires, which are fixed at one end and freely arranged at its other end and align themselves when voltage is applied along the field lines formed thereby. By moving the wires, adhering particles can easily be shaken off. For this purpose, a voltage can be applied several times in succession at short intervals, so that the wires move accordingly and shake off particles.
- the heating system is characterized in that for generating energy by burning an energy source such as biomass with a particulate matter emitting heating system, such as a biomass heating system, for burning the energy carrier, wherein particle-containing exhaust gases are formed, and comprising an electrostatic precipitator in an exhaust pipe a flow channel having a channel wall and a channel inside through which the particulate containing exhaust gas flows in a flow direction, an electrode extending substantially in the channel interior in the flow direction, and an electrode lead for feeding the electrode, the electrode lead being at least partially encased with an insulator ,
- the electrostatic precipitator is formed according to the electrostatic precipitator according to the invention, with a Pumbleabweisesch, which prevents particles of the exhaust gas abla at the electrode gladly.
- the method according to the invention is characterized in that in the method for reducing deposits of particles of an exhaust gas stream on an electric field generating electrode of an electrostatic precipitator of a heating system, comprising the steps of: generating an electric field between a channel wall and the electrode around It is provided that the step of moving the electrode flowing particles along the field lines from the exhaust gas stream, further comprising the step of: generating an electric ramp to upstream particles in the electric field to the electrode upstream of field lines of the electric apron a pre-electrode for generating the electric apron to move.
- the method further comprises the step of: moving at least one of the electrodes to shake off particles adhered to the corresponding electrode.
- the movement may be rotational, translatory (e.g., vibrating), or a combination thereof.
- the movement takes place jerkily.
- the polarity of the (middle) pre-electrode of the apron is preferably chosen to be identical to that of the downstream central or corona electrode.
- a charging unit there is an optimal distance between corona and pre-electrode or their optimal geometry (length, width, cross section, etc.).
- a metallic body which may be formed, for example, as a thickening of the electrode, electrically conductively connected to the electrode. The body is therefore at the same voltage level as the electrode.
- the body or pre-electrode which thus functions as a sacrificial electrode, preferably provides a much larger deposition surface than the center electrode of the charging unit. As a result, the maximum operating time of the electrostatic precipitator can be extended to functional restrictions and thus a next maintenance section.
- the electrostatic precipitator according to the invention has a minimal flow resistance in an exhaust gas system, which increases only slightly and slowly even as the loading of adhering particles increases. Electrostatic precipitators have a relatively large absorption capacity for separated particulate matter of the particle flow. At slow flow velocities of the exhaust gas stream and sufficiently long separation distances for the fine dust, electrostatic precipitators for submicron particles have a separation efficiency> 90%. For the reasons explained above, therefore, electrostatic precipitators are often used for the exhaust gas purification of heating systems such as a pellet heating system, other biomass heating systems or oil burners. Maintaining the necessary for the charging of the particles corona current even after several hours of operation is a technical difficulty in the design of the electrostatic precipitator. Keeping the invention lying at high voltage potential center electrode keeps the maximum operating time of the electrostatic precipitator until the next maintenance crucial.
- the pre-electrode is formed as an extension of the charging electrode to a thicker end against the flow direction of the exhaust gas. This tail serves as a "sacrificial electrode" with a much larger loading capacity for charged particulate matter than the (middle) electrode.
- the automated cleaning concept for the corona electrode has the following effects: Numerous tests have shown that the fine dust from wood combustion, for example, adheres very loosely to the corona electrode. The movement of the electrode, or parts thereof, forced by the alignment of the wires in the electrostatic field is sufficient to shake off the particulate matter. This movement is easy to automate.
- Fig. 1 schematically shows a longitudinal cross-section through an embodiment of an electrostatic precipitator 1 according to the invention.
- the electrostatic precipitator 1 is arranged in an exhaust pipe 2 (only partially shown) of an exhaust gas purification system not shown here and comprises a flow channel 3.
- the flow channel 3 is formed as a tubular portion of the exhaust pipe 2 and comprises a channel wall 4 and a channel interior 5.
- a particle-containing exhaust gas represented here by an arrow P flows in the flow direction likewise represented by the arrow P.
- an electrode 6, which is also referred to as a center electrode or corona electrode extends in the interior of the flow channel 3.
- the flow channel 3 is preferably formed in cross-section in the flow direction P rotationally symmetrical about a central axis A.
- the electrode 6 extends along this central axis A.
- the electrode 6 is fed via an electrode feed 7, which is covered with an insulator 8.
- the electrode 6 forms a charging unit, in which particles can be charged electrically.
- the electrode 6 forms with the channel wall 4 under application of a high voltage an electric field whose field lines are substantially radial to the electrode 6 and the channel wall 4, substantially transversely, more precisely at right angles to the flow direction P. upstream in the flow direction P.
- the electrode 6 is a Vorelektrodeniser 9 with a pre-electrode 10 is arranged.
- This pre-electrode unit 9 has the same polarity as the electrode 6, but at a different voltage level.
- the pre-electrode 10 is electrically conductively connected to the electrode 6, wherein in the illustrated embodiment, the pre-electrode 10 is formed in the shape different from the electrode 6, more precisely as a thickening of the electrode 6.
- the pre-electrode 10 forms with the corresponding portion of the channel wall 4 when applying a voltage a corresponding apron. In this apron, particles which would arrive without the apron to the electrode 6, to the pre-electrode 10th directed.
- the pre-electrode 10 has a larger capacity than the electrode 6 by their larger surface area. In this way, a longer service life of the electrostatic precipitator 1 is ensured.
- FIGS. 2 and 3 shows an embodiment of an electrode 6 or 10, with which adhering particles can be removed from the electrode 6 and 10, respectively.
- Fig. 2A-B show schematically in a side view an embodiment of a tuft-like electrode 6 and 10, once without electric field ( Fig. 2A ), once in an existing electric field ( Fig. 2B ).
- the tuft-like electrode 6, 10 has a plurality of electrically conductive wires 11.
- the wires 11 are clamped at one of their ends fixed in a holder 12. The other, opposite end of the wires 11 is free.
- Fig. 2A There is no electric field.
- the wires 11 align according to the gravitational field.
- Fig. 2B an electric field is applied. Accordingly, the electrically conductive wires 11 align according to the field lines of this generated field.
- the wires 11 of the electrode 6, 10 can be moved. Due to this movement, particles adhering to the wires 11 can be shaken off.
- FIGS. 3A and 3B show schematically in a plan view of the embodiment according to Fig. 2A or 2B.
- Fig. 3A is a state without generated electric field to see the alignment of the wires 11 can not recognize this in this illustration.
- Fig. 3B on the other hand, an electric field is applied and the wires 11 are aligned in accordance with the field lines of the field extending radially from the electrode 6, 10.
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Abstract
Description
Die Erfindung betrifft einen elektrostatischen Abscheider, insbesondere für eine Abgasleitung einer Abgasreinigungsanlage, nach dem Oberbegriff des Patentanspruches 1. Weiter betrifft die Erfindung ein Heizungssystem zur Erzeugung von Energie mittels Verbrennen von einem Energieträger mit einem elektrostatischen Abscheider nach dem Oberbegriff des Patentanspruchs 7. Darüber hinaus betrifft die Erfindung ein Verfahren zur Reduzierung von Ablagerungen von Partikeln eines Abgasstroms an einer ein elektrisches Feld erzeugenden Elektrode eines elektrostatischen Abscheiders eines Heizungssystems nach dem Oberbegriff des Patentanspruchs 8.The invention relates to an electrostatic precipitator, in particular for an exhaust pipe of an exhaust gas purification system, according to the preamble of claim 1. Furthermore, the invention relates to a heating system for generating energy by burning an energy source with an electrostatic precipitator according to the preamble of claim 7. In addition concerns the invention a method for reducing deposits of particles of an exhaust gas flow to an electric field generating electrode of an electrostatic precipitator of a heating system according to the preamble of
Die
Die
Aufgrund der Emissionen von Heizungsanlagen und globaler Bemühungen, derartige Emissionen zu reduzieren - siehe zum Beispiel das Kyoto-Abkommen - werden bei Heizungsanlagen entsprechende Abgasreinigungsanlagen verwendet. Diese sollen insbesondere die schädlichen Stoffe und Partikel aus Abgasen herausfiltern, so dass das verbleibende, gereinigte Abgas bedenkenlos an die Umwelt abgegeben werden kann. Insbesondere werden derartige Abgasreinigungsanlagen bei Biomasse-Heizanlagen eingesetzt, bei denen neben ansonsten ökonomischen und ökologischen Vorteilen eine erhöhte Emission an Schadstoffen in den Abgasen auftreten kann. Gerade die relativ hohe Emission an Feinstaub als ein Schadstoffanteil ist bei Biomasse-Heizungsanlagen ein Problem.Due to emissions from heating systems and global efforts to reduce such emissions - see, for example, the Kyoto Protocol - heating systems use appropriate emission control systems. These are in particular to filter out the harmful substances and particles from exhaust gases, so that the remaining, purified exhaust gas can be safely released to the environment. In particular, such emission control systems in biomass heating systems used in addition to otherwise economic and environmental benefits increased emissions of pollutants in the exhaust gases can occur. Especially the relatively high emission of particulate matter as a pollutant component is a problem in biomass heating systems.
Aus der
Ein derartiger Elektrofilter mit Sprühelektrode und Kollektorelektrode ist auch als elektrostatischer Abscheider bekannt. Dieser wird zur Abgasreinigung in einer Abgasleitung einer Heizungsanlage eingesetzt. Dabei wird durch die Sprühelektrode, welche etwa mittig durch die Abgasleitung verläuft und deshalb auch als Mittelelektrode bezeichnet wird, und eine umgebende Mantelfläche der Abgasleitung ein Kondensator gebildet, der bei einer zylinderrohrförmigen Ausbildung der Abgasleitung auch als Zylinderkondensator bezeichnet wird. Die Sprüh- oder Mittelelektrode weist in der Regel einen kreisförmigen Querschnitt in Strömungsrichtung des Abgases auf, wobei der Durchmesser des Querschnitts oder auch der Krümmungsradius im Allgemeinen relativ klein ausgebildet ist (zum Beispiel kleiner als 0,4 mm). Um nun die Schadstoffe, genauer die nicht an die Umwelt abzugebenden Partikel, des Abgases aus dem Abgasstrom abzuscheiden, wird durch die Mittelelektrode und die durch die Mantelfläche gebildete Kollektorelektrode ein quer zur Strömungsrichtung verlaufendes Feld mit Feldlinien von der Mittelelektrode zur Kollektorelektrode gebildet. Hierzu wird an die Mittelelektrode eine Hochspannung angelegt, zum Beispiel in dem Bereich von 15 kV. Dadurch bildet sich eine Corona-Entladung aus, durch welche die in dem Abgas durch das Feld strömenden Partikel unipolar aufgeladen werden. Aufgrund dieser Aufladung wandern die meisten der Partikel durch die elektrostatischen Coulomb-Kräfte zur Innenwand der Abgasleitung, welche als Kollektorelektrode dient.Such an electrostatic filter with a spray electrode and a collector electrode is also known as an electrostatic precipitator. This is used for exhaust gas purification in an exhaust pipe of a heating system. In this case, a capacitor is formed by the spray, which runs approximately centrally through the exhaust pipe and therefore also referred to as the center electrode, and a peripheral surface of the exhaust pipe, which is also referred to as a cylindrical capacitor in a cylindrical tube-shaped design of the exhaust pipe. The spray or center electrode generally has a circular cross section in the flow direction of the exhaust gas, wherein the diameter of the cross section or the radius of curvature is generally formed relatively small (for example, less than 0.4 mm). In order now to deposit the pollutants, more precisely the particles not to be discharged to the environment, of the exhaust gas from the exhaust gas flow, a field extending transversely to the flow direction is formed by field lines from the center electrode to the collector electrode through the center electrode and the collector electrode formed by the lateral surface. For this purpose, a high voltage is applied to the center electrode, for example in the range of 15 kV. As a result, a corona discharge is formed, through which the particles flowing through the field in the exhaust gas are charged in a unipolar manner. Due to this charge, most of the particles migrate through the electrostatic Coulomb forces to the inner wall of the exhaust pipe, which serves as a collector electrode.
Wie oben bereits erwähnt, werden die Partikel durch die entlang der Oberfläche der Elektrode sich ausbildende Corona-Entladung elektrostatisch aufgeladen. Dies geschieht auf molekularer Ebene durch folgenden Prozess: Liegt die Elektrode z.B. gegenüber dem Abgasrohr auf negativer Hochspannung, so wird eine große Anzahl von Gasmolekülen negativ aufgeladen. Sie bewegen sich im von der Elektrode sowie dem Abgasrohr aufgespannten elektrischen Feld in Richtung des Abgasrohres. Treffen diese auf ihrem Weg durch das Abgasrohr auf elektrisch neutrale Partikel, so bleiben sie an diesen haften und laden die bis dahin neutralen Partikel ebenfalls negativ auf. Die geladenen Partikel strömen getrieben durch elektrostatische Ablenkungskräfte zur Innenwand des Abgasrohres. Hier bleiben die Teilchen haften, verlieren ihre Ladung und werden sicher aus dem Abgasstrom entfernt. Dies ist der Kernprozess eines elektrostatischen Abscheiders und führt je nach Geometrie, Höhe des Corona-Stroms, Elektrodenform etc. zu Abscheideraten bis etwa über 90%. Dieser Kernprozess kann durch folgende Effekte gestört werden:As mentioned above, the particles are electrostatically charged by the corona discharge which forms along the surface of the electrode. this happens At the molecular level, by the following process: If, for example, the electrode is at a negative high voltage relative to the exhaust pipe, a large number of gas molecules will be negatively charged. They move in the electric field applied by the electrode and the exhaust pipe in the direction of the exhaust pipe. If these meet on their way through the exhaust pipe to electrically neutral particles, they stick to these and charge the previously neutral particles also negative. The charged particles flow driven by electrostatic deflection forces to the inner wall of the exhaust pipe. Here the particles stick, lose their charge and are safely removed from the exhaust stream. This is the core process of an electrostatic precipitator and, depending on the geometry, height of the corona current, electrode shape, etc., leads to deposition rates of up to more than 90%. This core process can be disturbed by the following effects:
Bei der Verbrennung entstehen bipolar geladene Partikel. Mittels Boltzmann-Verteilung kann der Anteil einfach bzw. mehrfach geladener Partikel abgeschätzt werden. Die Verteilung ist symmetrisch, d.h. es entstehen gleich viele positive wie negativ geladene Partikel. Für Bedingungen, wie sie im Abgas von Biomasse-Heizungen vorliegen, tragen zwischen 15 und 20% der Partikel eine elektrische Elementarladung. Die Anzahl geladener Partikel wird durch Koagulation zwar um ca. 10% pro Sekunde reduziert, dennoch liegen am Ort des elektrostatischen Abscheiders (entspricht ca. ein bis zwei Sekunden Flugzeit der Partikel vom Ort der Verbrennung) noch über 10% geladener Partikel vor. Gelangen die geladenen Partikel nun in die Nähe der auf negative Hochspannung liegenden Elektrode der Aufladeeinheit (Einheit Abgasrohr, Elektrode), so werden die negativen Partikel von der Elektrode weg in Richtung Abgasrohrinnenseite strömen. Die positiven Partikel strömen dagegen auf die Elektrode zu. Hiervon wird ein Teil beim Durchströmen der Aufladeeinheit neutralisiert bzw. negativ umgeladen, der Rest der Partikel gelangt jedoch zur Elektrode und lagert sich dort ab. Über die Betriebsdauer kommt es deshalb zu Funktionseinschränkungen des elektrostatischen Abweisers. Denn der auf der Elektrode abgelagerte Feinstaub verhindert lokal die Ausbildung der Corona. Dadurch verschlechtert sich die elektrische Aufladung der Partikel. Die Abscheideeffizienz des Systems wird degradiert. Zudem existiert in unmittelbarer Nähe der Corona (in einem Radius wenige Millimeter um die Elektrode) ein bipolares Ladungsgebiet. Elektrisch neutrale Partikel, welche dieses Gebiet durchströmen, können auch von einer negativen Elektrode positiv aufgeladen werden. Sie strömen dann auf die Elektrode zu. Ein Teil wird durch die Corona neutralisiert bzw. negativ umgeladen, ein kleiner Rest gelangt jedoch zur Elektrode und lagert sich ebenfalls dort ab.Burning produces bipolar charged particles. By means of Boltzmann distribution, the proportion of single or multiply charged particles can be estimated. The distribution is symmetrical, ie there are the same number of positive and negatively charged particles. For conditions such as those present in the exhaust gas of biomass heating systems, between 15 and 20% of the particles carry an elementary electric charge. Although the number of charged particles is reduced by approx. 10% per second due to coagulation, there are still more than 10% charged particles at the electrostatic precipitator (corresponding to about one to two seconds of particle flying time from the place of combustion). Now get the charged particles in the vicinity of the lying on negative high voltage electrode of the charger (unit exhaust pipe, electrode), the negative particles will flow away from the electrode towards the exhaust pipe inside. The positive particles, on the other hand, flow towards the electrode. Of this, a part is neutralized or negatively charged while flowing through the charger, but the rest of the particles reaches the electrode and deposits there. Over the service life it comes therefore to function restrictions of the electrostatic deflector. Because the fine dust deposited on the electrode locally prevents the formation of the corona. As a result, the electrical charge of the particles deteriorates. The deposition efficiency of the system is degraded. In addition, in the immediate vicinity of the corona (within a radius of a few millimeters around the electrode) there is a bipolar charge area. Electrically neutral particles which flow through this area can also be positively charged by a negative electrode. They then flow to the electrode. One part is neutralized or negatively charged by the corona, but a small remainder reaches the electrode and also deposits there.
Nachteilig an den elektrostatischen Abscheidern gemäß dem Stand der Technik ist, dass es nach einer längeren Betriebszeit zu einer kontinuierlichen Degradation des Corona-Stroms bei konstanter Hochspannung kommt. Dadurch sinkt die Aufladeeffizienz der Elektrode, was wiederum die Abscheideleistung des gesamten Systems verringert.A disadvantage of the electrostatic precipitators according to the prior art is that it comes after a longer period of operation to a continuous degradation of the corona current at a constant high voltage. As a result, the charging efficiency of the electrode decreases, which in turn reduces the separation efficiency of the entire system.
Der Erfindung liegt die Aufgabe zugrunde, einen elektrostatischen Abscheider zu schaffen, der diesen Nachteil überwindet und der insbesondere eine Ablagerung von Partikeln auf der Elektrode verhindert oder reduziert, um die Funktionsdauer des elektrostatischen Abscheiders zu erhöhen.The invention has for its object to provide an electrostatic precipitator, which overcomes this disadvantage and in particular prevents or reduces the deposition of particles on the electrode to increase the service life of the electrostatic precipitator.
Weiter liegt der Erfindung die Aufgabe zugrunde, ein Heizungssystem mit einem erfindungsgemäßen Abscheider zu schaffen, das eine zuverlässige Abgasreinigung garantiert.Further, the invention has for its object to provide a heating system with a separator according to the invention, which guarantees reliable exhaust gas purification.
Zudem liegt der Erfindung die Aufgabe zugrunde, ein Verfahren zu schaffen, nach welchem die dauerhafte Ablagerung von Partikeln an der Elektrode verhindert oder zumindest reduziert wird.In addition, the invention has for its object to provide a method according to which the permanent deposition of particles on the electrode is prevented or at least reduced.
Erfindungsgemäß wird dies durch die Gegenstände mit den Merkmalen des Patentanspruches 1 und des Patentanspruchs 7 sowie durch ein Verfahren mit den Merkmalen gemäß des Patentanspruchs 8 gelöst. Vorteilhafte Weiterbildungen sind den Unteransprüchen zu entnehmen.This is achieved by the objects with the features of claim 1 and of claim 7 and by a method having the features according to
Der erfindungsgemäße elektrostatische Abscheider ist dadurch gekennzeichnet, dass bei dem elektrostatischen Abscheider, insbesondere für eine Abgasleitung einer Abgasreinigungsanlage, mit einem Strömungskanal mit einer Kanalwandung und einem Kanalinneren, durch welchen ein partikelbeinhaltendes Abgas in einer Strömungsrichtung strömt, und einer sich in dem Kanalinneren im Wesentlichen in Strömungsrichtung erstreckenden Elektrode, zur Bildung eines elektrischen Feldes zwischen Elektrode und der Kanalwandung, vorgesehen ist, dass weiter ein Partikelabweisemittel umfasst ist, welches verhindert, dass sich Partikel des Abgases an der Elektrode ablagern. Das Partikelabweisemittel verhindert oder reduziert wirksam ein Ablagern von Partikeln an der Elektrode.The electrostatic precipitator according to the invention is characterized in that in the electrostatic precipitator, in particular for an exhaust pipe of an exhaust gas purification system, with a flow channel having a channel wall and a channel inside, through which a particle-containing exhaust gas flows in a flow direction, and in the channel interior substantially in Provided flow direction extending electrode, for forming an electric field between the electrode and the channel wall, is provided that further comprises a Partikelabweisemittel is included, which prevents particles of the exhaust gas to deposit on the electrode. The particle repelling agent effectively prevents or reduces the deposition of particles on the electrode.
In einer Ausführungsform ist vorgesehen, dass das Partikelabweisemittel mindestens eine Vorelektrodeneinheit umfasst, welche in Strömungsrichtung des Abgases vor der Elektrode angeordnet ist, um eine elektrisches Feld in Strömungsrichtung vor der Elektrode zu bilden.In an embodiment, it is provided that the particle-repelling means comprises at least one pre-electrode unit, which is arranged in front of the electrode in the flow direction of the exhaust gas in order to form an electric field in the flow direction in front of the electrode.
Aufgrund dieses Feldes werden Partikel, welche entlang ihrer Strömung das elektrische Feld der Vorelektrodeneinheit passieren, vorgelagert zu der Elektrode, zumindest zu einem Großteil, wirksam aus dem Abgasstrom entfernt. Partikel die ohne Vorelektrodeneinheit zur Elektrode gelangen würden, werden somit wirksam vor der Elektrode herausgefiltert.Due to this field, particles which pass along their flow the electric field of the Vorelektrodeneinheit, upstream of the electrode, at least for the most part, effectively removed from the exhaust gas flow. Particles that would reach the electrode without Vorelektrodeneinheit are thus effectively filtered out in front of the electrode.
In einer weiteren Ausführungsform ist vorgesehen, dass die Vorelektrodeneinheit so ausgebildet ist, dass diese ein zu der Elektrode gleiches Spannungsniveau benutzt. An der Vorelektrodeneinheit kann aber auch ein zu der Elektrode unterschiedliches Spannungsniveau angelegt sein, welches höher oder niedriger als das der Elektrode ist. Hiermit wird eine wirksame Filterfunktion realisiert.In a further embodiment it is provided that the pre-electrode unit is designed such that it uses a voltage level which is the same as the electrode. On the Vorelektrodeneinheit but also a different voltage level to the electrode may be applied, which is higher or lower than that of the electrode. This realizes an effective filter function.
In noch einer weiteren Ausführungsform ist vorgesehen, dass die Vorelektrodeneinheit eine Vorelektrode aufweist, welche die gleiche Polarität wie die Elektrode besitzt. Auf diese Weise wird sichergestellt, dass Partikel, welche ohne Vorelektrodeneinheit zur Elektrode gelangen würden, an der vorgelagerten Vorelektrodeneinheit zu der Vorelektrode gelangen. Die Vorelektrode wirkt somit als eine Art "Opferelektrode".In yet another embodiment, it is provided that the pre-electrode unit has a pre-electrode which has the same polarity as the electrode. In this way, it is ensured that particles which would reach the electrode without a pre-electrode unit reach the pre-electrode at the upstream pre-electrode unit. The pre-electrode thus acts as a kind of "sacrificial electrode".
Ein Ausführungsbeispiel sieht vor, dass die Vorelektrode als leitend verbunden mit der Elektrode ausgebildet ist. Auf diese Weise ist sichergestellt, dass Elektrode und Vorelektrode die gleiche Polarität aufweisen.An embodiment provides that the pre-electrode is formed as conductively connected to the electrode. This ensures that the electrode and the pre-electrode have the same polarity.
Noch ein weiteres Ausführungsbeispiel sieht vor, dass die Vorelektrode unterschiedlich zu der Elektrode ausgebildet ist. Die Vorelektrode ist insbesondere hinsichtlich der für die Erzeugung eines elektrischen Feldes erforderlichen Parameter unterschiedlich zu der Elektrode ausgebildet. Die Unterschiede können in der Geometrie, dem Material, dem Herstellungsverfahren, der Oberflächenstruktur und dergleichen ausgebildet sein. Die Vorelektrode ist in einer bevorzugten Ausführungsform einteilig mit der Elektrode ausgebildet. Bevorzugt ist die Vorelektrode gegenüber der Elektrode als Verdickung ausgebildet.
Eine Ausführungsform der Erfindung sieht vor, dass mindestens eine der Elektroden zumindest teilweise als büschelartige Anordnung von Drähten ausgebildet ist, welche an einem Ende fest und an ihrem anderen Ende frei angeordnet sind und sich bei Anlegen einer Spannung entlang der dadurch gebildeten Feldlinien ausrichten. Durch Bewegen der Drähte können anhaftende Partikel einfach abgeschüttelt werden. Hierzu kann eine Spannung mehrfach hintereinander in kurzen Abständen angelegt werden, so dass die Drähte sich entsprechend bewegen und Partikel abschütteln.Yet another embodiment provides that the pre-electrode is formed differently from the electrode. The pre-electrode is formed differently from the electrode, in particular with regard to the parameters required for generating an electric field. The differences may be in geometry, material, manufacturing method, surface structure, and the like. The pre-electrode is formed in one preferred embodiment in one piece with the electrode. Preferably, the pre-electrode is formed with respect to the electrode as a thickening.
An embodiment of the invention provides that at least one of the electrodes is at least partially formed as a tuft-like arrangement of wires, which are fixed at one end and freely arranged at its other end and align themselves when voltage is applied along the field lines formed thereby. By moving the wires, adhering particles can easily be shaken off. For this purpose, a voltage can be applied several times in succession at short intervals, so that the wires move accordingly and shake off particles.
Das Heizungssystem ist dadurch gekennzeichnet, dass zur Erzeugung von Energie mittels Verbrennen von einem Energieträger wie Biomasse mit einer Feinstaub emittierenden Heizungsanlage, wie einer Biomasse-Heizungsanlage, zum Verbrennen des Energieträgers, wobei partikelbeinhaltende Abgase entstehen, und mit einem elektrostatischen Abscheider in einer Abgasleitung, umfassend einen Strömungskanal mit einer Kanalwandung und einem Kanalinneren, durch welchen das partikelbeinhaltende Abgas in einer Strömungsrichtung strömt, eine sich in dem Kanalinneren im Wesentlichen in Strömungsrichtung erstreckende Elektrode und eine Elektrodenzuführung, um die Elektrode zu speisen, wobei die Elektrodenzuführung mit einem Isolator zumindest teilweise ummantelt ist, vorgesehen ist, dass der elektrostatische Abscheider gemäß dem erfindungsgemäßen elektrostatischen Abscheider ausgebildet ist, mit einem Partikelabweisemittel, welches verhindert, dass sich Partikel des Abgases an der Elektrode ablagern.The heating system is characterized in that for generating energy by burning an energy source such as biomass with a particulate matter emitting heating system, such as a biomass heating system, for burning the energy carrier, wherein particle-containing exhaust gases are formed, and comprising an electrostatic precipitator in an exhaust pipe a flow channel having a channel wall and a channel inside through which the particulate containing exhaust gas flows in a flow direction, an electrode extending substantially in the channel interior in the flow direction, and an electrode lead for feeding the electrode, the electrode lead being at least partially encased with an insulator , It is provided that the electrostatic precipitator is formed according to the electrostatic precipitator according to the invention, with a Partikelabweisemittel, which prevents particles of the exhaust gas abla at the electrode gladly.
Das erfindungsgemäße Verfahren ist dadurch gekennzeichnet, dass bei dem Verfahren zur Reduzierung von Ablagerungen von Partikeln eines Abgasstroms an einer ein elektrisches Feld erzeugenden Elektrode eines elektrostatischen Abscheiders eines Heizungssystems, umfassend die Schritte: Erzeugen eines elektrischen Feldes zwischen einer Kanalwandung und der Elektrode, um die entlang der Elektrode strömenden Partikel entlang der Feldlinien aus dem Abgasstrom zu bewegen, vorgesehen ist, dass weiter der Schritt umfasst ist: Erzeugen eines elektrischen Vorfeldes, um Partikel, die sich in dem elektrischen Feld zu der Elektrode bewegen, vorgelagert entlang von Feldlinien des elektrischen Vorfeldes zu einer Vorelektrode zur Erzeugung des elektrischen Vorfeldes zu bewegen.The method according to the invention is characterized in that in the method for reducing deposits of particles of an exhaust gas stream on an electric field generating electrode of an electrostatic precipitator of a heating system, comprising the steps of: generating an electric field between a channel wall and the electrode around It is provided that the step of moving the electrode flowing particles along the field lines from the exhaust gas stream, further comprising the step of: generating an electric ramp to upstream particles in the electric field to the electrode upstream of field lines of the electric apron a pre-electrode for generating the electric apron to move.
In einer Ausführungsform umfasst das Verfahren weiter den Schritt: Bewegen mindestens einer der Elektroden, um an der entsprechenden Elektrode anhaftende Partikel abzuschütteln. Die Bewegung kann rotatorisch, translatorisch (z.B. vibrierend) oder als Kombination davon erfolgen. Bevorzugt erfolgt die Bewegung ruckartig.In an embodiment, the method further comprises the step of: moving at least one of the electrodes to shake off particles adhered to the corresponding electrode. The movement may be rotational, translatory (e.g., vibrating), or a combination thereof. Preferably, the movement takes place jerkily.
Mit dem erfindungsgemäßen elektrostatischen Abscheider, dem erfindungsgemäßen Heizungssystem und dem erfindungsgemäßen Verfahren werden insbesondere die folgenden Vorteile realisiert:With the electrostatic precipitator according to the invention, the heating system according to the invention and the method according to the invention, in particular the following advantages are realized:
Eine Vermeidung bzw. Reduzierung von Feinstaubablagerungen auf der Elektrode wird realisiert. Damit die positiv geladenen Partikel im Abgasstrom sich nicht auf der Elektrode ablagern können, müssen sie aus der Abgasströmung entfernt werden. Dies geschieht vorliegend durch ein zweites elektrisches (Vor-) Feld stromaufwärts vor der Elektrode.An avoidance or reduction of fine dust deposits on the electrode is realized. So that the positively charged particles in the exhaust gas stream can not be deposited on the electrode, they must be removed from the exhaust gas flow. This is done in the present case by a second electric (pre-) field upstream of the electrode.
Dieses kann durch eine getrennte Hochspannungszuführung auf einem anderen Spannungsniveau wie jenes der (Mittel-) Elektrode realisiert werden. Die Polarität der (Mittel-)Vorelektrode des Vorfeldes wird dabei vorzugsweise identisch wie die der nachgeschalteten Mittel- oder Corona-Elektrode gewählt. Abhängig von der Strömungsgeschwindigkeit bzw. der Geometrie der Einheit Elektrode-Abgasrohr, welche auch als Aufladungseinheit bezeichnet wird, existiert ein optimaler Abstand zwischen Corona- und Vorelektrode bzw. deren optimale Geometrie (Länge, Breite, Querschnitt etc.). Stromaufwärts zur Aufladungseinheit ist ein metallischer Körper, der zum Beispiel als Verdickung der Elektrode ausgebildet sein kann, elektrisch leitend mit der Elektrode verbunden. Der Körper liegt daher auf demselben Spannungsniveau wie die Elektrode. Durch eine entsprechende Dimensionierung des Körpers bzw. der Elektroden kann erreicht werden, dass an dem Körper oder der Vorelektrode zuverlässig alle aus dem Verbrennungsprozess stammenden positiv geladenen Partikel abgeschieden werden. Der Körper oder die Vorelektrode, welche somit als "Opfer-Elektrode" fungiert, bietet bevorzugt eine viel größere Ablagerungsfläche als die Mittelelektrode der Aufladungseinheit. Dadurch kann die maximale Betriebszeit des elektrostatischen Abscheiders bis zu Funktionseinschränkungen und somit einem nächsten Wartungsabschnitt verlängert werden.This can be realized by a separate high voltage supply at a different voltage level as that of the (middle) electrode. The polarity of the (middle) pre-electrode of the apron is preferably chosen to be identical to that of the downstream central or corona electrode. Depending on the flow velocity or the geometry of the unit electrode-exhaust pipe, which is also referred to as a charging unit, there is an optimal distance between corona and pre-electrode or their optimal geometry (length, width, cross section, etc.). Upstream of the charging unit is a metallic body, which may be formed, for example, as a thickening of the electrode, electrically conductively connected to the electrode. The body is therefore at the same voltage level as the electrode. By appropriate dimensioning of the body or of the electrodes, it is possible to reliably deposit all positively charged particles originating from the combustion process on the body or the pre-electrode. The body or pre-electrode, which thus functions as a sacrificial electrode, preferably provides a much larger deposition surface than the center electrode of the charging unit. As a result, the maximum operating time of the electrostatic precipitator can be extended to functional restrictions and thus a next maintenance section.
Eine automatisierte Entfernung von Verunreinigungen auf der Hochspannungselektrode wird realisiert. Trotz des elektrischen Vorfeldes kann es zu Feinstaubablagerungen auf der Elektrode kommen. Diese lassen sich automatisiert entfernen. Es hat sich gezeigt, dass statt einer massiven drahtförmigen Elektrode auch ein Büschel aus feinen Drähtchen bei Anlegen einer Hochspannung einen ausreichend hohen Corona-Strom erzeugt. Die feinen Drähte sind ausreichend beweglich, so dass sie bei Aufschalten der Hochspannung den elektrischen Feldlinien folgen. Bei Ausschalten der Hochspannung folgen die Drähte wieder der Gravitation. Durch entsprechendes Schalten bewegen sich die Drähte hin und her. Diese Bewegung reicht aus, um den locker anhaftenden Feinstaub abzuschütteln. Falls die Bewegung in der Gasströmung nicht ausreichend ausgeprägt erfolgt, so kann auch bei Stillstand des Abgasventilators mehrmals automatisiert die Hochspannung ein- und ausgeschaltet werden. Die feinen Drähte unterliegen im aggressiven Plasma der Corona natürlich auch einem erhöhten chemischen und physikalischen Verschleiß. Durch entsprechend angepasste Geometrie- und Materialauswahl wird das Optimum zwischen Ausbildung eines ausreichend hohen Corona-Stroms, der elektrostatischen Beweglichkeit und chemisch-physikalischer Beständigkeit eingestellt.Automated removal of contaminants on the high voltage electrode is realized. Despite the electric ramp, it can lead to fine dust deposits on the electrode. These can be removed automatically. It has been shown that instead of a solid wire-shaped electrode, a tuft of fine wires generates a sufficiently high corona current when a high voltage is applied. The fine wires are sufficiently mobile that they follow the electric field lines when the high voltage is applied. When the high voltage is switched off, the wires follow the gravitation again. By appropriate switching, the wires move back and forth. This movement is sufficient to shake off the loosely adhering fine dust. If the movement in the gas flow is not sufficiently pronounced, the high voltage can be switched on and off several times automatically even when the exhaust fan is at a standstill. The fine wires are naturally also subject to increased chemical and physical wear in the aggressive plasma of the corona. By appropriate geometry and material selection, the optimum is set between the formation of a sufficiently high corona current, the electrostatic mobility and chemical-physical resistance.
Der erfindungsgemäße elektrostatische Abscheider weist in einem Abgassystem einen minimalen Strömungswiderstand auf, welcher sich auch bei steigender Beladung durch anhaftende Partikeln nur geringfügig und langsam erhöht. Elektrostatische Abscheider weisen eine relativ große Aufnahme-Kapazität für abgeschiedenen Feinstaub des Partikelstroms auf. Bei langsamen Strömungsgeschwindigkeiten des Abgasstroms und genügend langen Abscheidestrecken für den Feinstaub, verfügen elektrostatische Abscheider für submikrone Partikel über eine Abscheideeffizienz > 90%. Aus den zuvor ausgeführten Gründen werden elektrostatische Abscheider deshalb häufig für die Abgasreinigung von Heizungssystemen wie einer Pellet-Heizanlage, anderen Biomasse-Heizanlagen oder Ölbrennern eingesetzt. Das Aufrechterhalten des für die Aufladung der Partikel nötigen Corona-Stroms auch nach mehreren Betriebsstunden stellt eine technische Schwierigkeit bei der Ausführung des elektrostatischen Abscheiders dar. Das erfindungsgemäße Freihalten der auf Hochspannungspotential liegenden Mittelelektrode verlängert die maximale Betriebszeit des elektrostatischen Abscheiders bis zur nächsten Wartung entscheidend.The electrostatic precipitator according to the invention has a minimal flow resistance in an exhaust gas system, which increases only slightly and slowly even as the loading of adhering particles increases. Electrostatic precipitators have a relatively large absorption capacity for separated particulate matter of the particle flow. At slow flow velocities of the exhaust gas stream and sufficiently long separation distances for the fine dust, electrostatic precipitators for submicron particles have a separation efficiency> 90%. For the reasons explained above, therefore, electrostatic precipitators are often used for the exhaust gas purification of heating systems such as a pellet heating system, other biomass heating systems or oil burners. Maintaining the necessary for the charging of the particles corona current even after several hours of operation is a technical difficulty in the design of the electrostatic precipitator. Keeping the invention lying at high voltage potential center electrode keeps the maximum operating time of the electrostatic precipitator until the next maintenance crucial.
Das elektrische Vorfeld gleicher Polarität aber von optimiertem Spannungsniveau, welches stromaufwärts zur eigentlichen Aufladeeinheit angeordnet ist, entfernt bei geeigneter Wahl der Geometrie zuverlässig alle bereits geladen aus dem Verbrennungsprozess stammenden Feinstaubpartikel. Dadurch wird die Elektrode der Aufladungseinheit zuverlässig von Feinstaub freigehalten. In einer Ausführungsform ist die Vorelektrode als Verlängerung der Aufladungselektrode um ein dickeres Endstück entgegen der Strömungsrichtung des Abgases ausgebildet. Dieses Endstück dient als "Opferelektrode" mit einer sehr viel größeren Beladungskapazität für geladene Feinstaubpartikel als die (Mittel-) Elektrode.The electric apron of the same polarity but of optimized voltage level, which is arranged upstream of the actual charging unit, reliably removes all already loaded from the combustion process fine dust particles with a suitable choice of geometry. As a result, the electrode of the charging unit is reliably kept free of fine dust. In one embodiment, the pre-electrode is formed as an extension of the charging electrode to a thicker end against the flow direction of the exhaust gas. This tail serves as a "sacrificial electrode" with a much larger loading capacity for charged particulate matter than the (middle) electrode.
Das automatisierte Reinigungskonzept für die Corona-Elektrode wirkt wie folgt: In zahlreichen Versuchen hat sich gezeigt, dass der Feinstaub aus zum Beispiel der Holzverbrennung sehr locker an der Corona-Elektrode haftet. Die durch das Ausrichten der Drähte im elektrostatischen Feld erzwungene Bewegung der Elektrode, oder Teilen davon, ist ausreichend um den Feinstaub abzuschütteln. Dieses Bewegen lässt sich einfach automatisieren.The automated cleaning concept for the corona electrode has the following effects: Numerous tests have shown that the fine dust from wood combustion, for example, adheres very loosely to the corona electrode. The movement of the electrode, or parts thereof, forced by the alignment of the wires in the electrostatic field is sufficient to shake off the particulate matter. This movement is easy to automate.
Die Zeichnungen stellen mehrere Ausführungsbeispiele der Erfindung dar und zeigen in den Figuren:
- Fig. 1
- schematisch einen Längsquerschnitt durch eine Ausführungsform eines erfindungsgemäßen elektrostatischen Abscheiders,
- Fig.2A-B
- schematisch in einer Seitenansicht ein Ausführungsbeispiel einer büschelartigen Elektrode, einmal ohne elektrisches Feld (2A), einmal mit angelegtem elektrischen Feld (2b), und
- Fig. 3A-B
- schematisch in einer Draufsicht das Ausführungsbeispiel gemäß
Fig. 2A und 2B .
- Fig. 1
- FIG. 2 schematically shows a longitudinal cross section through an embodiment of an electrostatic precipitator according to the invention, FIG.
- 2A-B
- schematically in a side view an embodiment of a tuft-like electrode, once without electric field (2A), once with an applied electric field (2b), and
- Fig. 3A-B
- schematically in a plan view of the embodiment according to
FIGS. 2A and 2B ,
Claims (9)
dadurch gekennzeichnet, dass weiter ein Partikelabweisemittel umfasst ist, welches verhindert, dass sich Partikel des Abgases (P) an der Elektrode (6) ablagern, wobei das Partikelabweisemittel mindestens eine Vorelektrodeneinheit (9) umfasst, welche in Strömungsrichtung des Abgases (P) vor der Elektrode (6) angeordnet ist, um ein elektrisches Feld in Strömungsrichtung (P) vor der Elektrode (6) zu bilden.Electrostatic separator (1), in particular for an exhaust pipe (2) of an exhaust gas purification system, comprising a flow channel (3) having a channel wall (4) and a channel interior (5) through which a particle-containing exhaust gas (P) flows in a flow direction, and one in the channel interior (5) substantially in the flow direction (P) extending electrode (6), to form an electric field between the electrode (6) and the channel wall (4),
characterized in that further comprises a Partikelabweisemittel is included, which prevents particles of the exhaust gas (P) to deposit on the electrode (6), wherein the Partikelabweisemittel comprises at least one Vorelektrodeneinheit (9), which in the flow direction of the exhaust gas (P) in front of the Electrode (6) is arranged to form an electric field in the flow direction (P) in front of the electrode (6).
dadurch gekennzeichnet, dass die Vorelektrodeneinheit (9) so ausgebildet ist, dass diese ein zu der Elektrode (6) gleiches Spannungsniveau benutzt.Electrostatic separator (1) according to claim 1,
characterized in that the pre-electrode unit (9) is formed to use a voltage level equal to the electrode (6).
dadurch gekennzeichnet, dass die Vorelektrodeneinheit (9) eine Vorelektrode (10) aufweist, welche die gleiche Polarität wie die Elektrode (6) besitzt.Electrostatic separator (1) according to claim 1 or 2,
characterized in that the pre-electrode unit (9) has a pre-electrode (10) which has the same polarity as the electrode (6).
dadurch gekennzeichnet, dass die Vorelektrode (10) leitend verbunden mit der Elektrode (6) ausgebildet ist.Electrostatic separator (1) according to one of claims 1 to 3,
characterized in that the pre-electrode (10) is conductively connected to the electrode (6).
dadurch gekennzeichnet, dass die Vorelektrode (10) unterschiedlich zu der Elektrode (6) ausgebildet ist.Electrostatic precipitator (1) according to one of claims 1 to 4,
characterized in that the pre-electrode (10) is formed differently from the electrode (6).
dadurch gekennzeichnet, dass mindestens eine der Elektroden (6,10) zumindest teilweise als büschelartige Anordnung von Drähten (11) ausgebildet ist, welche an einem Ende fest und an ihrem anderen Ende frei angeordnet sind und sich bei Anlegen einer Spannung entlang der dadurch begründeten Feldlinien ausrichten.Electrostatic separator (1) according to one of claims 1 to 5,
characterized in that at least one of the electrodes (6,10) is at least partially formed as a tuft-like arrangement of wires (11) which are fixed at one end and freely disposed at its other end and upon application of a voltage along the thereby established field lines align.
dadurch gekennzeichnet, dass der elektrostatische Abscheider (1) nach einem der Ansprüche 1 bis 6 ausgebildet ist mit einem Partikelabweisemittel, welches verhindert, dass sich Partikel des Abgases (P) an der Elektrode (6) ablagern.Heating system for generating energy by burning an energy source such as biomass with a particulate matter emitting heating system, such as a biomass heating system, for burning the energy carrier, wherein particulate exhaust gases (P) are formed, and an electrostatic precipitator (1) in an exhaust pipe (2) comprising a flow channel (3) having a channel wall (4) and a channel interior (5) through which the particle-containing exhaust gas (P) flows in a flow direction, an electrode extending in the channel interior (5) substantially in the flow direction (P) (6) and an electrode feed (7) for feeding at least the electrode (6), wherein the electrode feed (7) is at least partially encased with an insulator (8),
characterized in that the electrostatic precipitator (1) according to any one of claims 1 to 6 is formed with a Partikelabweisemittel, which prevents particles of the exhaust gas (P) from depositing on the electrode (6).
dadurch gekennzeichnet, dass weiter der Schritt umfasst ist: Bewegen mindestens einer der Elektroden (6, 10), um an der entsprechenden Elektrode (6, 10) anhaftende Partikel abzuschütteln.Method according to claim 8,
characterized by further comprising the step of: moving at least one of the electrodes (6, 10) to shake off particles adhering to the respective electrode (6, 10).
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112090247A (en) * | 2020-10-31 | 2020-12-18 | 张家港市金秋环保科技有限公司 | Electric field line tensioning adjusting device and tensioning adjusting method |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102009021072A1 (en) * | 2009-05-13 | 2010-11-25 | Robert Bosch Gmbh | Electrostatic separator and heating system |
CN108397776B (en) * | 2018-03-27 | 2020-11-03 | 安徽工业大学 | Method for shunting treatment and emission reduction of dioxin in incineration flue gas |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2045647A (en) | 1979-03-28 | 1980-11-05 | Burgess Mfg Air Cleaners Ltd | Ionizing devices |
JPH04301117A (en) | 1991-03-28 | 1992-10-23 | Teikoku Piston Ring Co Ltd | Particulate separating device |
EP1193445A2 (en) | 2000-10-02 | 2002-04-03 | Eidgenössische Materialprüfungs- und Forschungsanstalt Empa | Device to clean exhausts from small heating systems |
JP2007263754A (en) | 2006-03-28 | 2007-10-11 | Shimadzu Corp | Emission spectrometer |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7332019B2 (en) * | 2005-08-17 | 2008-02-19 | American Standard International Inc. | Air filtration system |
-
2007
- 2007-11-24 DE DE200710056696 patent/DE102007056696B3/en not_active Expired - Fee Related
-
2008
- 2008-11-08 EP EP08019567.0A patent/EP2062649B1/en active Active
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2045647A (en) | 1979-03-28 | 1980-11-05 | Burgess Mfg Air Cleaners Ltd | Ionizing devices |
JPH04301117A (en) | 1991-03-28 | 1992-10-23 | Teikoku Piston Ring Co Ltd | Particulate separating device |
EP1193445A2 (en) | 2000-10-02 | 2002-04-03 | Eidgenössische Materialprüfungs- und Forschungsanstalt Empa | Device to clean exhausts from small heating systems |
JP2007263754A (en) | 2006-03-28 | 2007-10-11 | Shimadzu Corp | Emission spectrometer |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112090247A (en) * | 2020-10-31 | 2020-12-18 | 张家港市金秋环保科技有限公司 | Electric field line tensioning adjusting device and tensioning adjusting method |
CN112090247B (en) * | 2020-10-31 | 2023-01-17 | 张家港市金秋环保科技有限公司 | Electric field line tensioning adjusting device and tensioning adjusting method |
Also Published As
Publication number | Publication date |
---|---|
EP2062649B1 (en) | 2016-01-27 |
DE102007056696B3 (en) | 2009-05-07 |
EP2062649A3 (en) | 2013-07-17 |
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