EP1769851A1 - Electrostatic precipitator - Google Patents

Electrostatic precipitator Download PDF

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Publication number
EP1769851A1
EP1769851A1 EP05021046A EP05021046A EP1769851A1 EP 1769851 A1 EP1769851 A1 EP 1769851A1 EP 05021046 A EP05021046 A EP 05021046A EP 05021046 A EP05021046 A EP 05021046A EP 1769851 A1 EP1769851 A1 EP 1769851A1
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EP
European Patent Office
Prior art keywords
filter
filter device
electrodes
gas turbine
gas
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Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Application number
EP05021046A
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German (de)
French (fr)
Inventor
Miroslav Dr. Podhorsky
Thomas Dr. Riepe
Timo Seppaelae
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Balcke Duerr GmbH
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Balcke Duerr GmbH
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Priority to EP05021046A priority Critical patent/EP1769851A1/en
Priority to US11/527,717 priority patent/US20080072759A1/en
Publication of EP1769851A1 publication Critical patent/EP1769851A1/en
Withdrawn legal-status Critical Current

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION 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
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/019Post-treatment of gases
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION 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
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/02Plant or installations having external electricity supply
    • B03C3/025Combinations of electrostatic separators, e.g. in parallel or in series, stacked separators, dry-wet separator combinations
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION 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
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/02Plant or installations having external electricity supply
    • B03C3/04Plant or installations having external electricity supply dry type
    • B03C3/14Plant or installations having external electricity supply dry type characterised by the additional use of mechanical effects, e.g. gravity
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION 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
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/34Constructional details or accessories or operation thereof
    • B03C3/40Electrode constructions
    • B03C3/45Collecting-electrodes
    • B03C3/49Collecting-electrodes tubular

Definitions

  • the invention relates to a filter device for separating particles from a gas fluid aspirated by a gas turbine and a gas turbine with such a filter device.
  • a compressor from the surrounding air sucks, compresses and directs them to a combustion chamber of the gas turbine. There, the air is burned together with a supplied fuel, resulting in hot combustion gases. The combustion gases flow at high speed into a turbine which is driven therewith.
  • dirt particles When sucking the air from the environment of the gas turbine compressor, it is unavoidable that dirt particles are introduced into the compressor with.
  • the dirt particles can sand grains, insects, pollen, dust of different chemical composition u. ⁇ . Have. In the compressor, they encounter rotating parts, which can lead to unwanted reactions. These include erosion or corrosion of compressor blades, deposits on the compressor blades and other parts inside the compressor, or agglomerations and chemical reactions of the supplied foreign bodies with each other.
  • the operation of a textile filter can be problematic, since forming a wet surface of the filter ice, thus a flow passage is significantly hampered and a gas turbine is only partially operable.
  • the textile filters used are regularly replaced with new and clean filters, to achieve a long life of the gas turbine, the associated compressor including the compressor blades are cleaned several times a year. Since in this case the gas turbine, which is usually in operation without interruption, must be switched off and power generation by the gas turbine is thus interrupted, such maintenance measures are complex and expensive.
  • the invention is therefore an object of the invention to provide a filter device of the type mentioned above, which has a low pressure loss between the input and output side of the filter device at a high filter effect, so that a high gas turbine performance is achievable, this being both dry and should be possible in humid ambient air.
  • a time-consuming maintenance and cleaning of the filter device should no longer be necessary.
  • the filter device for separating particles from a gas fluid aspirated by a gas turbine has a vertically arranged pipe electrostatic filter.
  • dirt particles are electrically charged in the gas fluid and transported by the action of electrical forces to an electrode on which they are deposited. Since the gas fluid no longer needs to flow through any meshes of a textile filter, this filtering is coupled with a low pressure loss between the inlet and outlet sides of the filter device, so that even large gas fluid streams can be efficiently filtered.
  • the charging of dirt particles succeeds even with moist gas fluid, so that can be achieved on the output side of the filter, a dry fluid.
  • the frequency of maintenance operations for cleaning compressor blades and the like will become less frequent. a. significantly reduced, and the erosion and corrosion of compressor blades is reduced. Due to the low pressure loss, a compressor can be sized smaller and a larger gas turbine performance can be achieved.
  • the tubular electrostatic filter of the filter device for ionization of the particles in the gas fluid needle-shaped sputtering electrodes, which generate overlapping ion beams.
  • This can generate a strong turbulence of the ion beams, slowed down by the dirt particles in the gas fluid and effectively to one for the deposition provided electrode can be transported. This makes it possible to achieve a high deposition rate of the dirt particles.
  • a voltage of greater than 130 kV is present between a positive and a negative electrode of the tubular electro-filter.
  • a relatively large distance between the electrodes can be achieved, so that the pressure loss during the passage of the filter is even lower.
  • larger tolerances for a deposited amount of dust on a collecting electrode can be allowed by the greater distance of the electrodes. This makes it possible to increase a time interval between individual cycles for cleaning such a filter. Furthermore, such a high voltage enables an even higher deposition rate and thus a very efficient filtering effect.
  • the tube electrostatic precipitator may comprise a filter cell having a honeycomb-shaped precipitation electrode for the deposition of the contaminant particles, wherein the precipitation electrode is arranged around the ejection electrodes.
  • the honeycomb structure allows a self-supporting structure of the filter device, so that a lightweight construction can be achieved. This reduces the manufacturing costs of the filter device according to the invention.
  • the filter device is provided with a tubular electrostatic filter having 1, 3, 4, 7, 10, 16, 25, 36, 45, 55, 65 or 95 filter cells.
  • the filter cells are arranged in parallel, so that can be filtered by such a modular design of the filter device very small to very large volume flows efficiently.
  • the filter device according to the invention is preferably designed such that a dry or wet cleaning of the electrodes can be carried out in the tubular electrostatic filter.
  • a suitable cleaning of the electrodes can be carried out.
  • this cleaning is preferably carried out by a mechanically induced vibration of the electrodes. This can be done for example in such a way that the electrodes hit impact tools regularly, whereby the dust is released from the electrode surfaces and drops. If the operating voltage is briefly lowered during knocking, the cleaning can be improved.
  • the electrodes are, for example, sprayed with water and the resulting sludge flushed out.
  • the filter device has at least one additional filter, which is connected downstream of the tube electrostatic precipitator.
  • This may be a plate electrostatic filter with relatively narrow lanes intended for dry gas fluid.
  • the additional filter takes over a "monitoring function", so that there is additional security with regard to a low entry of dirt particles into the compressor in the case of possibly not well filtered gas fluid through the tubular electrostatic filter.
  • a textile filter can be provided.
  • This is advantageous because the contamination of the textile filter can be reduced to a minimum by the upstream tubular electrostatic filter, so that the hitherto known difficulties, such as frequent maintenance, no longer occur in a textile filter downstream of the tubular electrostatic precipitator.
  • a moist gas fluid After passing through the tubular electrostatic precipitator, a moist gas fluid has already been freed from moisture to such an extent that no clumping or clogging of filter meshes occurs in the textile filter.
  • This is also advantageous when operating the filter in winter, because the dirt particles on the textile filter can not freeze and a passage of gas fluid is no longer blocked.
  • the textile filter is also advantageous because it can be operated without the supply of electrical energy, so that sufficient energy can still be obtained for a limited time when the electrical energy that is not present can be reached.
  • the invention further relates to a gas turbine with a compressor, a combustion chamber and a turbine, wherein the gas turbine has a filter device, as has been previously described.
  • FIG. 1 schematically shows a gas turbine 100.
  • air 1 is sucked from the outside and passes through a filter device 2.
  • the filter device 2 has in this embodiment, a tubular electrostatic precipitator 20 and a downstream textile filter 22, which are shown in Figure 1 only schematically.
  • the tubular electrostatic precipitator is intended to provide, in a first stage filter, high filtration, even from a humid gas fluid, e.g. To reach air.
  • the downstream textile filter is thus supplied dried air, so that clogging of dirt particles does not occur and a good air passage is given.
  • the filtered air enters the compressor 3 and is compressed there until it exits at its outlet as compressed air 4 again. There it is passed to a combustion chamber 5, where it is burned together with a supplied fuel 7.
  • combustion gases 8 which are passed to a downstream turbine 9 and drive the turbine.
  • the flow energy of the combustion gas 8 is partially converted to mechanical energy by driving the compressor 3 and a generator 12.
  • the compressor 3 and the turbine 9 as well as the generator 12 are mounted on a common shaft 13. After passing through the turbine 9, the combustion gas 8 finally exits the turbine 9 as hot exhaust gas 10.
  • the efficiency of a gas turbine can be increased by using the heat of the hot exhaust gas 10. This is done, for example, in that the hot exhaust gas 10 is supplied to a recuperator 5 (heat exchanger), which preheats the compressed air 4 before it enters the combustion chamber 8, see Fig. 2. Thus, the amount of fuel supplied. 7 reduce, so that less energy is required to operate the gas turbine. Less hot exhaust gas 11 then exits the recuperator 5.
  • a recuperator 5 heat exchanger
  • FIG. 3 shows a top view of a tubular electro-filter 20 which is used in the filter device according to the invention.
  • the tubular electrostatic precipitator 20 has discharge electrodes 21 which project in a needle-shaped manner in the direction of the precipitation electrode 23 surrounding it.
  • the sputtering electrodes are cathodically poled, so that when a voltage is applied by the sputtering electrode, electrons are emitted. They experience such a strong acceleration that, starting from a certain voltage, an ionization of the gasfluid surrounding and to be filtered by the discharge electrodes occurs. This ionization occurs well below the breakdown voltage.
  • the free electrons strike neutral gas molecules, so that gas ions and other electrons are formed by impact ionization. This forms an electron avalanche, which moves towards the collecting electrode. If the spray electrodes are close enough to each other, the gas ion beams 22 overlap, as shown in FIG. On the one hand, the gas ions strike the collecting electrode and release more electrons on impact. On the other hand, the gas ions deposit on dust particles and load them with it. Under the influence of the electric field between the electrodes, the charged dust particles are transported transversely to the flow direction of the fluid to the collecting electrode where they release their charges and deposit on their surface due to adhesive forces, so that a deposited dust layer 24 is formed (in Fig.
  • the deposition electrode should be designed such that to achieve a nearly constant electric field between a spray electrode and an associated deposition electrode, the distance between the electrodes is approximately equal.
  • the collecting electrode is honeycombed or formed as a hexagonal tube. This is advantageous in particular with regard to the joining together of a plurality of filter cells 25, see FIG. 4. This makes it possible to achieve a self-supporting structure of the filter device without a gap between the individual cells, which requires relatively little material and is nevertheless stable.
  • the honeycomb structure makes it possible to achieve a larger or smaller passage area for the fluid to be filtered by combining a desired number of filter cells.

Abstract

An electrostatic filter unit (2) for removing particles from a gaseous fluid sucked into a gas turbine comprises a vertically arranged tube electro-filter (20) and at least one additional textile filter (22) arranged after the electro-filter. Preferably the electro-filter comprises needle-shaped ionizing electrodes that produced overlapping ion beams to ionize the particles. An independent claim is also included for a gas turbine comprising the above filter.

Description

Die Erfindung betrifft eine Filtervorrichtung zum Abscheiden von Partikeln aus einem von einer Gasturbine angesaugten Gasfluid und eine Gasturbine mit einer solchen Filtervorrichtung.The invention relates to a filter device for separating particles from a gas fluid aspirated by a gas turbine and a gas turbine with such a filter device.

Bei einer Gasturbine saugt ein Verdichter aus der Umgebung Luft an, verdichtet diese und leitet sie zu einer Brennkammer der Gasturbine. Dort wird die Luft zusammen mit einem zugeführten Brennstoff verbrannt, wodurch heiße Verbrennungsgase entstehen. Die Verbrennungsgase strömen mit hoher Geschwindigkeit in eine Turbine, welche damit angetrieben wird.In a gas turbine, a compressor from the surrounding air sucks, compresses and directs them to a combustion chamber of the gas turbine. There, the air is burned together with a supplied fuel, resulting in hot combustion gases. The combustion gases flow at high speed into a turbine which is driven therewith.

Beim Ansaugen der Luft aus der Umgebung des Gasturbinenverdichters ist es unvermeidbar, dass Schmutzpartikel in den Verdichter mit eingeführt werden. Die Schmutzpartikel können Sandkörner, Insekten, Pollen, Staub unterschiedlicher chemischer Zusammensetzung u. ä. aufweisen. Im Verdichter treffen sie auf rotierende Teile, wodurch unerwünschte Reaktionen die Folge sein können. Dazu gehören eine Erosion oder Korrosion von Verdichterschaufeln, Ablagerungen auf den Verdichterschaufeln und anderen Teilen im Innenbereich des Verdichters oder Zusammenballungen und chemische Reaktionen der zugeführten Fremdkörper miteinander.When sucking the air from the environment of the gas turbine compressor, it is unavoidable that dirt particles are introduced into the compressor with. The dirt particles can sand grains, insects, pollen, dust of different chemical composition u. Ä. Have. In the compressor, they encounter rotating parts, which can lead to unwanted reactions. These include erosion or corrosion of compressor blades, deposits on the compressor blades and other parts inside the compressor, or agglomerations and chemical reactions of the supplied foreign bodies with each other.

Um derartige Reaktionen in ihren Auswirkungen zu verringern, wird üblicherweise die angesaugte Luft vor dem Eintreten in den Verdichter mit einem Textilfilter gefiltert. Mit den derzeit verfügbaren Textilfiltern lässt sich eine sehr wirksame Filterung erreichen, so dass kaum noch Schmutzpartikel in den Innenbereich eines Verdichters eindringen können. Beim Einsatz derartiger Filter besteht jedoch das grundsätzliche Problem, dass mit zunehmender Filterwirkung ein Druckverlust einher geht, so dass stets ein Kompromiss zwischen Filtereffizienz und Wirkungsgrad der Gasturbine geschlossen werden muss. Darüber hinaus hat sich gezeigt, dass bei feuchter Umgebungsluft, zum Beispiel aufgrund von Nebel, die im Filter zurückgehaltenen Schmutzpartikel feucht werden, diese verklumpen, und somit die Luftdurchlässigkeit und Effizienz des Filters eingeschränkt wird, wodurch ein zusätzlicher Druckverlust im Verdichter unvermeidbar ist. Besonders bei Temperaturen unterhalb von 0 °C kann der Betrieb eines Textilfilters problematisch werden, da sich bei einer feuchten Oberfläche des Filters Eis bildet, somit ein Strömungsdurchtritt erheblich behindert wird und eine Gasturbine nur noch eingeschränkt betreibbar ist. Um diesen Wirkungen vorzubeugen, werden üblicherweise die eingesetzten Textilfilter regelmäßig durch neue und saubere Filter ausgetauscht, wobei zum Erzielen einer langen Lebensdauer der Gasturbine der zugehörige Verdichter einschließlich der Verdichterschaufeln mehrmals im Jahr gereinigt werden. Da hierbei die Gasturbine, welche üblicherweise ohne Unterbrechung in Betrieb ist, abgeschaltet werden muss und eine Energieerzeugung durch die Gasturbine somit unterbrochen wird, sind derartige Wartungsmaßnahmen aufwändig und kostenintensiv.In order to reduce such effects in their effects, usually the sucked air is filtered before entering the compressor with a textile filter. With the currently available textile filters, a very effective filtering can be achieved, so that hardly any dirt particles can penetrate into the interior of a compressor. When using such filters, however, there is the fundamental problem that with increasing filter effect, a pressure loss is accompanied, so that always a compromise between filter efficiency and efficiency of the gas turbine must be concluded. In addition, it has been shown that in humid ambient air, for example, due to fog, the particles of dirt retained in the filter become moist, they clump together, and thus the Air permeability and efficiency of the filter is limited, whereby an additional pressure loss in the compressor is unavoidable. Especially at temperatures below 0 ° C, the operation of a textile filter can be problematic, since forming a wet surface of the filter ice, thus a flow passage is significantly hampered and a gas turbine is only partially operable. To prevent these effects, usually the textile filters used are regularly replaced with new and clean filters, to achieve a long life of the gas turbine, the associated compressor including the compressor blades are cleaned several times a year. Since in this case the gas turbine, which is usually in operation without interruption, must be switched off and power generation by the gas turbine is thus interrupted, such maintenance measures are complex and expensive.

Der Erfindung liegt daher die Aufgabe zugrunde, eine Filtervorrichtung der oben genannten Art anzugeben, welche bei einer hohen Filterwirkung einen geringen Druckverlust zwischen der Eingangs- und Ausgangsseite der Filtervorrichtung aufweist, so dass damit eine hohe Gasturbinenleistung erreichbar ist, wobei dies sowohl bei trockener als auch bei feuchter Umgebungsluft möglich sein soll. Zusätzlich soll eine zeitintensive Wartung und Reinigung der Filtervorrichtung nicht mehr erforderlich sein.The invention is therefore an object of the invention to provide a filter device of the type mentioned above, which has a low pressure loss between the input and output side of the filter device at a high filter effect, so that a high gas turbine performance is achievable, this being both dry and should be possible in humid ambient air. In addition, a time-consuming maintenance and cleaning of the filter device should no longer be necessary.

Diese Aufgabe wird dadurch gelöst, dass die Filtervorrichtung zum Abscheiden von Partikeln aus einem von einer Gasturbine angesaugten Gasfluid ein vertikal angeordnetes Rohrelektrofilter aufweist. Bei einem solchen Filter werden Schmutzpartikel im Gasfluid elektrisch aufgeladen und durch Einwirkung elektrischer Kräfte zu einer Elektrode transportiert, auf welcher sie abgeschieden werden. Da das Gasfluid keine Maschen eines Textilfilters mehr durchströmen muss, ist diese Filterung mit einem geringen Druckverlust zwischen Eingangs- und Ausgangsseite der Filtervorrichtung gekoppelt, so dass auch große Gasfluidströme effizient filterbar sind. Die Aufladung von Schmutzpartikeln gelingt auch bei feuchtem Gasfluid, so dass sich an der Ausgangsseite des Filters ein trockenes Fluid erzielen lässt. Somit wird die Häufigkeit von Wartungsarbeiten zur Reinigung von Verdichterschaufeln u. a. erheblich reduziert, und die Erosion und Korrosion von Verdichterschaufeln wird vermindert. Durch den geringen Druckverlust kann ein Verdichter kleiner dimensioniert und eine größere Gasturbinenleistung erzielt werden.This object is achieved in that the filter device for separating particles from a gas fluid aspirated by a gas turbine has a vertically arranged pipe electrostatic filter. In such a filter dirt particles are electrically charged in the gas fluid and transported by the action of electrical forces to an electrode on which they are deposited. Since the gas fluid no longer needs to flow through any meshes of a textile filter, this filtering is coupled with a low pressure loss between the inlet and outlet sides of the filter device, so that even large gas fluid streams can be efficiently filtered. The charging of dirt particles succeeds even with moist gas fluid, so that can be achieved on the output side of the filter, a dry fluid. Thus, the frequency of maintenance operations for cleaning compressor blades and the like will become less frequent. a. significantly reduced, and the erosion and corrosion of compressor blades is reduced. Due to the low pressure loss, a compressor can be sized smaller and a larger gas turbine performance can be achieved.

Bei einer bevorzugten Ausführungsform der Erfindung weist das Rohrelektrofilter der Filtervorrichtung zur Ionisation der Partikel im Gasfluid nadelförmige Sprühelektroden auf, welche sich einander überlappende lonenstrahlen erzeugen. Damit lässt sich eine starke Turbulenz der lonenstrahlen erzeugen, durch die die Schmutzpartikel im Gasfluid abgebremst und wirksam zu einer für die Abscheidung vorgesehenen Elektrode befördert werden können. Damit lässt sich eine hohe Abscheiderate der Schmutzpartikel erzielen.In a preferred embodiment of the invention, the tubular electrostatic filter of the filter device for ionization of the particles in the gas fluid needle-shaped sputtering electrodes, which generate overlapping ion beams. This can generate a strong turbulence of the ion beams, slowed down by the dirt particles in the gas fluid and effectively to one for the deposition provided electrode can be transported. This makes it possible to achieve a high deposition rate of the dirt particles.

Dabei ist es vorteilhaft, wenn zwischen einer positiven und einer negativen Elektrode des Rohrelektrofilters eine Spannung von größer als 130 kV anliegt. Damit kann ein relativ großer Abstand zwischen den Elektroden erreicht werden, so dass der Druckverlust beim Durchströmen des Filters noch geringer wird. Außerdem können durch den größeren Abstand der Elektroden größere Toleranzen für eine abgeschiedene Staubmenge auf einer Niederschlagselektrode zugelassen werden. Damit lässt sich ein Zeitintervall zwischen einzelnen Zyklen zur Reinigung eines derartigen Filters vergrößern. Ferner wird durch eine derart hohe Spannung eine noch höhere Abscheiderate und damit eine sehr effiziente Filterwirkung ermöglicht.It is advantageous if a voltage of greater than 130 kV is present between a positive and a negative electrode of the tubular electro-filter. Thus, a relatively large distance between the electrodes can be achieved, so that the pressure loss during the passage of the filter is even lower. In addition, larger tolerances for a deposited amount of dust on a collecting electrode can be allowed by the greater distance of the electrodes. This makes it possible to increase a time interval between individual cycles for cleaning such a filter. Furthermore, such a high voltage enables an even higher deposition rate and thus a very efficient filtering effect.

Das Rohrelektrofilter kann eine Filterzelle mit einer wabenförmig ausgebildeten Niederschlagselektrode für die Abscheidung der Schmutzpartikel aufweisen, wobei die Niederschlagselektrode um die Sprühelektroden angeordnet ist. Die wabenförmige Struktur ermöglicht einen selbsttragenden Aufbau der Filtervorrichtung, so dass eine Leichtbaukonstruktion erreichbar ist. Dies verringert die Herstellkosten der erfindungsgemäßen Filtervorrichtung.The tube electrostatic precipitator may comprise a filter cell having a honeycomb-shaped precipitation electrode for the deposition of the contaminant particles, wherein the precipitation electrode is arranged around the ejection electrodes. The honeycomb structure allows a self-supporting structure of the filter device, so that a lightweight construction can be achieved. This reduces the manufacturing costs of the filter device according to the invention.

Bevorzugt ist die Filtervorrichtung mit einem Rohrelektrofilter versehen, der 1, 3, 4, 7, 10, 16, 25, 36, 45, 55, 65 oder 95 Filterzellen aufweist. Die Filterzellen sind dabei in Parallelschaltung angeordnet, so dass sich durch einen derart modularen Aufbau der Filtervorrichtung sehr kleine bis sehr große Volumenströme effizient filtern lassen.Preferably, the filter device is provided with a tubular electrostatic filter having 1, 3, 4, 7, 10, 16, 25, 36, 45, 55, 65 or 95 filter cells. The filter cells are arranged in parallel, so that can be filtered by such a modular design of the filter device very small to very large volume flows efficiently.

Die erfindungsgemäße Filtervorrichtung ist vorzugsweise derart ausgebildet, dass in dem Rohrelektrofilter eine trockene oder nasse Abreinigung der Elektroden durchführbar ist. Damit kann je nach Verfügbarkeit von Reinigungsmedien eine geeignete Abreinigung der Elektroden durchgeführt werden. Ist eine trockene Abreinigung einer Elektrode vorgesehen, ist gemäß der Erfindung diese Abreinigung vorzugsweise durch eine mechanisch induzierte Vibration der Elektroden durchführbar. Dies kann zum Beispiel derart geschehen, dass auf die Elektroden regelmäßig Schlagwerkzeuge auftreffen, wodurch der Staub von den Elektrodenflächen gelöst wird und abfällt. Wird die Betriebsspannung während des Klopfens kurzzeitig gesenkt, kann die Abreinigung verbessert werden. Bei einer nassen Abreinigung werden die Elektroden zum Beispiel mit Wasser bedüst und der dann entstandene Schlamm ausgeschwemmt.The filter device according to the invention is preferably designed such that a dry or wet cleaning of the electrodes can be carried out in the tubular electrostatic filter. Thus, depending on the availability of cleaning media, a suitable cleaning of the electrodes can be carried out. If a dry cleaning of an electrode is provided, according to the invention, this cleaning is preferably carried out by a mechanically induced vibration of the electrodes. This can be done for example in such a way that the electrodes hit impact tools regularly, whereby the dust is released from the electrode surfaces and drops. If the operating voltage is briefly lowered during knocking, the cleaning can be improved. For wet cleaning, the electrodes are, for example, sprayed with water and the resulting sludge flushed out.

Bei einer weiteren Ausgestaltung der Erfindung weist die Filtervorrichtung mindestens ein zusätzliches Filter auf, welches dem Rohrelektrofilter nachgeschaltet ist. Dieses kann ein Plattenelektrofilter mit relativ engen Gassen sein, der für trockenes Gasfluid vorgesehen ist. Das zusätzliche Filter übernimmt eine "Überwachungsfunktion", so dass bei eventuell nicht gut gefiltertem Gasfluid durch das Rohrelektrofilter eine zusätzliche Sicherheit im Hinblick auf einen geringen Eintrag von Schmutzpartikeln in den Verdichter besteht.In a further embodiment of the invention, the filter device has at least one additional filter, which is connected downstream of the tube electrostatic precipitator. This may be a plate electrostatic filter with relatively narrow lanes intended for dry gas fluid. The additional filter takes over a "monitoring function", so that there is additional security with regard to a low entry of dirt particles into the compressor in the case of possibly not well filtered gas fluid through the tubular electrostatic filter.

Als zusätzliches Filter kann auch ein Textilfilter vorgesehen sein. Dies ist vorteilhaft, da sich durch das vorgeschaltete Rohrelektrofilter die Verschmutzung des Textilfilters auf ein Minimum reduzieren lässt, so dass die bisher bekannten Schwierigkeiten, wie zum Beispiel häufige Wartungsarbeiten, bei einem zum Rohrelektrofilter nachgeschalteten Textilfilter nicht mehr auftreten. Ein feuchtes Gasfluid ist nach Passieren des Rohrelektrofilters bereits so weit von Feuchtigkeit befreit, dass im Textilfilter kein Verklumpen oder Verstopfen von Filtermaschen mehr auftritt. Dies ist auch bei Betrieb des Filters im Winter vorteilhaft, da die Schmutzpartikel auf dem Textilfilter nicht mehr einfrieren können und ein Durchtritt von Gasfluid nicht mehr blockiert wird. Das Textilfilter ist zudem vorteilhaft, da es ohne Zufuhr elektrischer Energie betreibbar ist, so dass bei nicht vorhandener elektrischer Energie trotzdem für eine begrenzte Zeit eine ausreichende Filterung der vom Verdichter angesaugten Luft erreichbar ist.As an additional filter and a textile filter can be provided. This is advantageous because the contamination of the textile filter can be reduced to a minimum by the upstream tubular electrostatic filter, so that the hitherto known difficulties, such as frequent maintenance, no longer occur in a textile filter downstream of the tubular electrostatic precipitator. After passing through the tubular electrostatic precipitator, a moist gas fluid has already been freed from moisture to such an extent that no clumping or clogging of filter meshes occurs in the textile filter. This is also advantageous when operating the filter in winter, because the dirt particles on the textile filter can not freeze and a passage of gas fluid is no longer blocked. The textile filter is also advantageous because it can be operated without the supply of electrical energy, so that sufficient energy can still be obtained for a limited time when the electrical energy that is not present can be reached.

Die Erfindung betrifft ferner eine Gasturbine mit einem Verdichter, einer Brennkammer und einer Turbine, wobei die Gasturbine eine Filtervorrichtung aufweist, wie sie zuvor beschrieben worden ist.The invention further relates to a gas turbine with a compressor, a combustion chamber and a turbine, wherein the gas turbine has a filter device, as has been previously described.

Nachfolgend wird die Erfindung anhand von in der Zeichnung dargestellten Ausführungsbeispielen weiter beschrieben. Es zeigen:

Figur 1:
eine schematische Darstellung einer ersten Gasturbine mit einer erfindungsgemäßen Filtervorrichtung;
Figur 2:
eine schematische Darstellung einer zweiten Gasturbine mit einer erfindungsgemäßen Filtervorrichtung;
Figur 3:
eine Draufsicht einer ersten Ausführungsform der erfindungsgemäßen Filtervorrichtung mit einem vertikalen Rohrelektrofilter, und
Figur 4:
eine Draufsicht einer zweiten Ausführungsform der erfindungsgemäßen Filtervorrichtung mit mehreren Filterzellen.
The invention will be further described with reference to embodiments shown in the drawings. Show it:
FIG. 1:
a schematic representation of a first gas turbine with a filter device according to the invention;
FIG. 2:
a schematic representation of a second gas turbine with a filter device according to the invention;
FIG. 3:
a plan view of a first embodiment of the filter device according to the invention with a vertical Rohrelektrofilter, and
FIG. 4:
a plan view of a second embodiment of the filter device according to the invention with a plurality of filter cells.

In Figur 1 ist eine Gasturbine 100 schematisch dargestellt. Von einem Verdichter 3 wird Luft 1 von außen angesaugt und passiert eine Filtervorrichtung 2. Die Filtervorrichtung 2 weist bei dieser Ausführungsform ein Rohrelektrofilter 20 und ein nachgeschaltetes Textilfilter 22 auf, welche in Figur 1 nur schematisch dargestellt sind. Das Rohrelektrofilter ist dazu vorgesehen, in einer ersten Filterstufe eine hohe Filterung auch von einem feuchtem Gasfluid wie z.B. Luft zu erreichen. Dem nachgeschalteten Textilfilter wird somit getrocknete Luft zugeführt, so dass ein Verklumpen von Schmutzpartikeln nicht mehr auftritt und ein guter Luftdurchtritt gegeben ist. Die so gefilterte Luft tritt in den Verdichter 3 ein und wird dort verdichtet, bis sie an dessen Auslass als verdichtete Luft 4 wieder austritt. Dort wird sie zu einer Brennkammer 5 geleitet, wo sie zusammen mit einem zugeführten Brennstoff 7 verbrannt wird. Dabei entstehen Verbrennungsgase 8, die zu einer nachgeschalteten Turbine 9 geführt werden und die Turbine antreiben. Die Strömungsenergie des Verbrennungsgases 8 wird teilweise zu mechanischer Energie umgewandelt, indem der Verdichter 3 und ein Generator 12 angetrieben werden. Dazu sind der Verdichter 3 und die Turbine 9 wie auch der Generator 12 auf einer gemeinsamen Welle 13 gelagert. Das Verbrennungsgas 8 tritt nach Passieren der Turbine 9 schließlich als heißes Abgas 10 aus der Turbine 9 aus.FIG. 1 schematically shows a gas turbine 100. From a compressor 3, air 1 is sucked from the outside and passes through a filter device 2. The filter device 2 has in this embodiment, a tubular electrostatic precipitator 20 and a downstream textile filter 22, which are shown in Figure 1 only schematically. The tubular electrostatic precipitator is intended to provide, in a first stage filter, high filtration, even from a humid gas fluid, e.g. To reach air. The downstream textile filter is thus supplied dried air, so that clogging of dirt particles does not occur and a good air passage is given. The filtered air enters the compressor 3 and is compressed there until it exits at its outlet as compressed air 4 again. There it is passed to a combustion chamber 5, where it is burned together with a supplied fuel 7. This produces combustion gases 8, which are passed to a downstream turbine 9 and drive the turbine. The flow energy of the combustion gas 8 is partially converted to mechanical energy by driving the compressor 3 and a generator 12. For this purpose, the compressor 3 and the turbine 9 as well as the generator 12 are mounted on a common shaft 13. After passing through the turbine 9, the combustion gas 8 finally exits the turbine 9 as hot exhaust gas 10.

Der Wirkungsgrad einer Gasturbine kann gesteigert werden, indem die Wärme des heißen Abgases 10 genutzt wird. Dies erfolgt zum Beispiel dadurch, dass das heiße Abgas 10 einem Rekuperator 5 (Wärmetauscher) zugeführt wird, welcher die verdichtete Luft 4 vorwärmt, bevor sie in den Brennraum 8 gelangt, siehe Fig. 2. Damit gelingt es, die Menge des zugeführten Brennstoffes 7 zu verringern, so dass weniger Energie zum Betreiben der Gasturbine erforderlich ist. Weniger heißes Abgas 11 tritt anschließend aus dem Rekuperator 5 aus.The efficiency of a gas turbine can be increased by using the heat of the hot exhaust gas 10. This is done, for example, in that the hot exhaust gas 10 is supplied to a recuperator 5 (heat exchanger), which preheats the compressed air 4 before it enters the combustion chamber 8, see Fig. 2. Thus, the amount of fuel supplied. 7 reduce, so that less energy is required to operate the gas turbine. Less hot exhaust gas 11 then exits the recuperator 5.

In Fig. 3 ist eine Draufsicht eines Rohrelektrofilters 20 dargestellt, welches bei der erfindungsgemäßen Filtervorrichtung zum Einsatz kommt. Das Rohrelektrofilter 20 weist Sprühelektroden 21 auf, welche nadelförmig in Richtung zu der sie umgebenden Niederschlagselektrode 23 abstehen. Die Sprühelektroden sind kathodisch gepolt, so dass bei Anlegen einer Spannung von der Sprühelektrode Elektronen ausgesandt werden. Sie erfahren eine so starke Beschleunigung, dass ab einer bestimmten Spannung eine Ionisation des die Sprühelektroden umgebenden und zu filternden Gasfluides eintritt. Diese Ionisation erfolgt weit unterhalb der Durchbruchspannung.FIG. 3 shows a top view of a tubular electro-filter 20 which is used in the filter device according to the invention. The tubular electrostatic precipitator 20 has discharge electrodes 21 which project in a needle-shaped manner in the direction of the precipitation electrode 23 surrounding it. The sputtering electrodes are cathodically poled, so that when a voltage is applied by the sputtering electrode, electrons are emitted. They experience such a strong acceleration that, starting from a certain voltage, an ionization of the gasfluid surrounding and to be filtered by the discharge electrodes occurs. This ionization occurs well below the breakdown voltage.

Auf dem Weg von der Sprühelektrode zur Niederschlagselektrode treffen die freien Elektronen auf neutrale Gasmoleküle, so dass durch Stoßionisation Gasionen und weitere Elektronen entstehen. Damit bildet sich eine Elektronenlawine aus, welche sich auf die Niederschlagselektrode zubewegt. Sind die Sprühelektroden nahe genug beieinander, überlagern sich die Gasionenstrahlen 22, wie dies in Figur 3 dargestellt ist. Die Gasionen treffen zum einen auf die Niederschlagselektrode und setzen dort beim Auftreffen weitere Elektronen frei. Zum anderen lagern sich die Gasionen an Staubteilchen an und laden diese damit auf. Unter Einwirkung des elektrischen Feldes zwischen den Elektroden werden die aufgeladenen Staubteilchen quer zur Strömungsrichtung des Fluides zur Niederschlagselektrode transportiert, wo sie ihre Ladungen abgeben und sich auf deren Oberfläche aufgrund von Haftkräften ablagern, so dass eine abgeschiedene Staubschicht 24 gebildet wird (in Fig. 3 ist nur ein Teil der Niederschlagselektrodenfläche mit einer abgeschiedenen Schicht 24 dargestellt). Die gesamte Strömung, die sich von der Sprühelektrode zur Niederschlagselektrode zubewegt, wird als elektrischer Wind bezeichnet, wobei dieser Wind aus negativ geladenen Teilchen, neutralen Teilchen, Elektronen und Ionen besteht. Die erreichbare Stromstärke hängt unter anderem von dem Staubgehalt des zu reinigenden Gases und den bereits vorhanden Staubablagerungen auf den Elektroden ab.On the way from the spray electrode to the precipitation electrode, the free electrons strike neutral gas molecules, so that gas ions and other electrons are formed by impact ionization. This forms an electron avalanche, which moves towards the collecting electrode. If the spray electrodes are close enough to each other, the gas ion beams 22 overlap, as shown in FIG. On the one hand, the gas ions strike the collecting electrode and release more electrons on impact. On the other hand, the gas ions deposit on dust particles and load them with it. Under the influence of the electric field between the electrodes, the charged dust particles are transported transversely to the flow direction of the fluid to the collecting electrode where they release their charges and deposit on their surface due to adhesive forces, so that a deposited dust layer 24 is formed (in Fig. 3 is only part of the collecting electrode surface is shown with a deposited layer 24). The entire flow moving from the spray electrode to the precipitation electrode is called an electric wind, which wind consists of negatively charged particles, neutral particles, electrons and ions. The achievable amperage depends inter alia on the dust content of the gas to be cleaned and the already existing dust deposits on the electrodes.

Die Niederschlagselektrode sollte so gestaltet sein, dass zum Erzielen eines nahezu konstanten elektrischen Feldes zwischen einer Sprühelektrode und einer zugehörigen Niederschlagselektrode der Abstand zwischen den Elektroden ungefähr gleich ist.The deposition electrode should be designed such that to achieve a nearly constant electric field between a spray electrode and an associated deposition electrode, the distance between the electrodes is approximately equal.

Bei der in Fig. 3 dargestellten Ausführungsform des Rohrelektrofilters ist die Niederschlagselektrode wabenförmig bzw. als 6-Kant-Rohr ausgebildet. Dies ist besonders im Hinblick auf das Aneinanderfügen mehrerer Filterzellen 25 vorteilhaft, siehe Fig. 4. Damit lässt sich ohne Zwischenraum zwischen den einzelnen Zellen eine selbsttragende Struktur der Filtervorrichtung erreichen, die relativ wenig Material erfordert und trotzdem stabil ist. Durch die Wabenstruktur ist es einfach möglich, eine größere oder kleiner Durchtrittsfläche für das zu filternde Fluid zu erzielen, indem eine gewünschte Zahl von Filterzellen miteinander kombiniert werden.In the embodiment of the tubular electro-filter shown in FIG. 3, the collecting electrode is honeycombed or formed as a hexagonal tube. This is advantageous in particular with regard to the joining together of a plurality of filter cells 25, see FIG. 4. This makes it possible to achieve a self-supporting structure of the filter device without a gap between the individual cells, which requires relatively little material and is nevertheless stable. The honeycomb structure makes it possible to achieve a larger or smaller passage area for the fluid to be filtered by combining a desired number of filter cells.

Claims (11)

Filtervorrichtung (2) zum Abscheiden von Partikeln aus einem von einer Gasturbine angesaugten Gasfluid,
dadurch gekennzeichnet,
dass die Filtervorrichtung (2) ein vertikal angeordnetes Rohrelektrofilter (20) aufweist.
Filter device (2) for separating particles from a gas fluid aspirated by a gas turbine,
characterized,
that the filter device (2) comprises a vertically disposed tubular electric filter (20).
Filtervorrichtung (2) nach Anspruch 1,
dadurch gekennzeichnet,
dass das Rohrelektrofilter (20) zur Ionisation der Partikel im Gasfluid nadelförmige Sprühelektroden (21) aufweist, welche sich einander überlappende lonenstrahlen erzeugen.
Filter device (2) according to claim 1,
characterized,
in that the tubular electrostatic precipitator (20) for the ionization of the particles in the gas fluid has needle-shaped spray electrodes (21) which generate ion beams which overlap one another.
Filtervorrichtung (2) nach einem der Ansprüche 1 oder 2,
dadurch gekennzeichnet,
dass zwischen einer positiven und einer negativen Elektrode des Rohrelektrofilters (20) eine Spannung von größer als 130 kV anliegt.
Filter device (2) according to one of claims 1 or 2,
characterized,
in that a voltage of greater than 130 kV is applied between a positive and a negative electrode of the tubular electrostatic precipitator (20).
Filtervorrichtung (2) nach einem der Ansprüche 2oder 3,
dadurch gekennzeichnet,
dass das Rohrelektrofilter (20) eine Filterzelle (25) mit einer wabenförmig ausgebildeten Niederschlagselektrode (23) aufweist, welche um die Sprühelektroden (21) angeordnet ist.
Filter device (2) according to one of claims 2 or 3,
characterized,
in that the tubular electrostatic filter (20) has a filter cell (25) with a honeycomb-shaped precipitation electrode (23) which is arranged around the spray electrodes (21).
Filtervorrichtung (2) nach Anspruch 4,
dadurch gekennzeichnet,
dass das Rohrelektrofilter (20) 1, 3, 4, 7, 10, 16, 25, 36, 45, 55, 65 oder 95 Filterzellen (25) aufweist.
Filter device (2) according to claim 4,
characterized,
in that the tubular electrostatic filter (20) has 1, 3, 4, 7, 10, 16, 25, 36, 45, 55, 65 or 95 filter cells (25).
Filtervorrichtung (2) nach einem der Ansprüche 4 oder 5,
dadurch gekennzeichnet,
dass im Rohrelektrofilter (20) eine trockene oder nasse Abreinigung der Elektroden durchführbar ist.
Filter device (2) according to one of claims 4 or 5,
characterized,
in that a dry or wet cleaning of the electrodes can be carried out in the tubular electrostatic filter (20).
Filtervorrichtung (2) nach Anspruch 6,
dadurch gekennzeichnet,
dass eine trockene Abreinigung der Elektroden durch mechanisch induzierte Vibration der Elektroden durchführbar ist.
Filter device (2) according to claim 6,
characterized,
that a dry cleaning of the electrodes by mechanically induced vibration of the electrodes is feasible.
Filtervorrichtung (2) nach einem der Ansprüche 1 bis 7,
dadurch gekennzeichnet,
dass die Filtervorrichtung (2) mindestens ein zusätzliches Filter aufweist, welches dem Rohrelektrofilter (20) nachgeschaltet ist.
Filter device (2) according to one of claims 1 to 7,
characterized,
in that the filter device (2) has at least one additional filter which is connected downstream of the tubular electrostatic filter (20).
Filtervorrichtung (2) nach Anspruch 8,
dadurch gekennzeichnet,
dass als zusätzliches Filter ein Plattenelektrofilter vorgesehen ist.
Filter device (2) according to claim 8,
characterized,
that a plate electrostatic filter is provided as an additional filter.
Filtervorrichtung (2) nach einem der Ansprüche 8 oder 9,
dadurch gekennzeichnet,
dass als zusätzliches Filter ein Textilfilter (22) vorgesehen ist.
Filter device (2) according to one of claims 8 or 9,
characterized,
in that a textile filter (22) is provided as an additional filter.
Gasturbine (9) mit einem Verdichter (3), einer Brennkammer (5) und einer Turbine (9),
dadurch gekennzeichnet,
dass die Gasturbine (9) eine Filtervorrichtung (2) nach einem der Ansprüche 1 bis 10 aufweist.
Gas turbine (9) with a compressor (3), a combustion chamber (5) and a turbine (9),
characterized,
in that the gas turbine (9) has a filter device (2) according to one of claims 1 to 10.
EP05021046A 2005-09-27 2005-09-27 Electrostatic precipitator Withdrawn EP1769851A1 (en)

Priority Applications (2)

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