WO1995031270A1 - Device for detoxifying exhaust fumes from mobile equipments - Google Patents
Device for detoxifying exhaust fumes from mobile equipments Download PDFInfo
- Publication number
- WO1995031270A1 WO1995031270A1 PCT/DE1995/000618 DE9500618W WO9531270A1 WO 1995031270 A1 WO1995031270 A1 WO 1995031270A1 DE 9500618 W DE9500618 W DE 9500618W WO 9531270 A1 WO9531270 A1 WO 9531270A1
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- WIPO (PCT)
- Prior art keywords
- pipe system
- discharge
- dielectric
- pipe
- support plate
- Prior art date
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/92—Chemical or biological purification of waste gases of engine exhaust gases
- B01D53/94—Chemical or biological purification of waste gases of engine exhaust gases by catalytic processes
- B01D53/9445—Simultaneously removing carbon monoxide, hydrocarbons or nitrogen oxides making use of three-way catalysts [TWC] or four-way-catalysts [FWC]
- B01D53/9454—Simultaneously removing carbon monoxide, hydrocarbons or nitrogen oxides making use of three-way catalysts [TWC] or four-way-catalysts [FWC] characterised by a specific device
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/32—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by electrical effects other than those provided for in group B01D61/00
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/08—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
- B01J19/087—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing electric or magnetic energy
- B01J19/088—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing electric or magnetic energy giving rise to electric discharges
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/01—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust by means of electric or electrostatic separators
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/08—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/08—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
- F01N3/0892—Electric or magnetic treatment, e.g. dissociation of noxious components
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/08—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
- F01N3/10—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
- F01N3/24—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by constructional aspects of converting apparatus
- F01N3/28—Construction of catalytic reactors
- F01N3/2882—Catalytic reactors combined or associated with other devices, e.g. exhaust silencers or other exhaust purification devices
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01J—ELECTRIC DISCHARGE TUBES OR DISCHARGE LAMPS
- H01J37/00—Discharge tubes with provision for introducing objects or material to be exposed to the discharge, e.g. for the purpose of examination or processing thereof
- H01J37/32—Gas-filled discharge tubes
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01J—ELECTRIC DISCHARGE TUBES OR DISCHARGE LAMPS
- H01J37/00—Discharge tubes with provision for introducing objects or material to be exposed to the discharge, e.g. for the purpose of examination or processing thereof
- H01J37/32—Gas-filled discharge tubes
- H01J37/32009—Arrangements for generation of plasma specially adapted for examination or treatment of objects, e.g. plasma sources
- H01J37/32348—Dielectric barrier discharge
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/08—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
- B01J2219/0894—Processes carried out in the presence of a plasma
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/12—Improving ICE efficiencies
Definitions
- the invention relates to a device for the decontamination of exhaust gases from mobile systems, in which the exhaust gas passes through a plasma reactor which works according to the principle of dielectric barrier discharge and is formed from an arrangement of flat plates in which metallic and dielectric layers alternate, whereby discharge paths arranged spatially next to one another are formed.
- silent discharges are generated between electrodes, between which there is at least one dielectric layer or body, in such a way that a gas discharge is direct, i.e. from electrode to electrode, is not possible.
- Devices for generating stylish discharges are known from the prior art. Such devices are often used for ozonizers and usually have a coaxial geometry here.
- a device which serves to reduce pollutants in combustion exhaust gases, in which at least one reaction space is arranged in the exhaust gas duct, which is formed from metallic, parallel plates or concentric tubes and has a gap cross section has, wherein at least one plate or a tube of the reaction chamber is coated with an electrically insulating dielectric material. Furthermore, such a device is known from WO-A-92/19361, in which an exhaust gas is conducted into an annular space between an outer metal cylinder and an inner cylinder made of ceramic.
- the prior art in particular is concerned with clarifying the functioning of the method for detoxifying exhaust gases according to the principle of dielectric barrier discharge. Power plants on the one hand and also motor vehicles on the other hand are addressed there, the construction of the devices not being specified precisely.
- a compact design of the plasma reactor is imperative, particularly for use in mobile systems. At the same time, however, a large effective length and / or a large effective cross section of the reaction space should be ensured.
- the object is achieved according to the invention in a device of the type mentioned at the outset in that the discharge sections are connected in series in terms of flow and are arranged concentrically to one another, for which purpose two tube systems are nested coaxially one inside the other.
- the first pipe system preferably consists of at least three metallic pipes arranged coaxially on a support plate and the second pipe system consists of at least two pipes arranged coaxially on a support plate. These two pipe systems are nested to build the reactor.
- the second tube system which does not form an outer wall of the plasma reactor, is advantageously covered with a dielectric layer on the entire surface.
- both pipe systems can also be dielectrically coated on their sides facing the plasma.
- Figure 1 shows a plasma reactor in a sectional view
- Figures 2 and 3 the two pipe systems to build the
- FIG. 4 a section of the plasma reactor perpendicular to FIG. 1.
- FIG. 1 denotes a reactor which, according to FIGS. 2 and 3, consists of two pipe systems 10 and 20 which are nested coaxially one inside the other.
- the pipe system 10 consists, for example, of three metallic pipes 12, 13 and 14 arranged coaxially on an annular support plate 11.
- the inner pipe 12 breaks through the support plate 11 and serves as a gas inlet pipe. Its diameter is determined by the requirements of the exhaust gas generating system.
- the inside and outside diameters of the further tubes 13 and 14 are selected such that the radial distances a between the tubes 11 to 13 are equal to one another and that the tubes 11 to 13 of the tube system 10 are the same distance from those of the tube system 20 everywhere have s.
- the distances between the tubes 11 to 13 can be selected such that the cross section to be flowed through remains constant as a function of the distance R from the central axis, ie d ⁇ R - * - is.
- the striking distance of the silent discharge is specifically changed as a function of the radius.
- the outer diameter of the outer tube 14 is equal to the diameter of the support plate 11.
- the ends of the inner tubes 12 and 13 are at the same distance 1 from the support plate 11.
- the outer tube 14 extends beyond the tubes 12 and 13 so far, that the pipe system 20 takes place in the chamber 1 formed from the pipe system 10 and an end plate 30.
- the distance b between the ends of the pipe system 20 and the support plate 11 on the other hand, the distance c between the ends of the pipes 12 and 13 and the support plate 21 of the pipe system 20 and furthermore the distance d between the support plate 21 of the pipe system and the end plate 30 is equal to the lay length , so that applies
- the pipe system 20 according to FIG. 3 consists of metal parts and is covered on its entire inner and outer surface with a dielectric layer 28. It consists, for example, of two tubes 22 and 23 arranged coaxially on an annular support plate 21.
- the inner and outer diameters of the tubes 21 and 22 are chosen in FIG. 3 such that the radial distances e of the dielectric coated tubes are the same among one another and that the tubes of the tube system 20 have the same radial distance s everywhere as those of the tube system 10.
- the outer diameter of the outer tube 23 is equal to the diameter of the support plate 21.
- the distances m of the ends of the tubes 21 and 23 from the support plate are the same.
- the pipe system 20 is introduced into the pipe system in such a way that the spacing requirements mentioned when coating the pipe system 10 are met.
- the radial distance a of the tubes 14 and 23 is electrically nic 'ge it conductive spacers respects.
- the distances between the tubes 21 and 23 can be selected so that the cross-section to be flowed through as a function of the distance from the central axis either remains constant or that the stroke length s assumes different, particularly advantageous values.
- the support plate 21 is electrically conductively connected to a supply line 26 at a suitable point.
- the feed line is encased with a dielectric layer 28, which connects seamlessly to the dielectric sealing of the pipe system 20 and is led through the end plate 30 out of the reaction chamber.
- the end plate 30 has a. Gas outlet connection 31, the diameter of which is equal to the diameter of the gas inlet pipe 12.
- the pipe systems 10 and 20 are therefore electrodes between which a silent discharge can be operated.
- they are connected to a generator 40, which provides an electrical voltage with a suitable time profile, amplitude, frequency and / or pulse shape, pulse / pause ratio.
- the plasma reactor formed by the pipe systems is used in any, e.g. Flows through the exhaust gas in the direction indicated by the arrows in FIG. 1.
- the number of pipes of the pipe systems 10 and 20 given by way of example is not limited to three or two. Like the total length of the arrangement, it results from the desired degree of detoxification and from the input parameters.
- the pipe system not provided with a dielectric layer can be coated with a conventional catalyst material on the side facing the exhaust gas in order to achieve improved detoxification.
- the pipe system 10 can also have a dielectric on the side facing the exhaust gas. be coated trically.
- a ceramic catalyst material can take on the role of the dielectric.
- Such a material can consist, for example, of mixtures containing titanium oxide, vanadium oxide and tungsten oxide.
- both pipe systems 10 and 20 of FIG. 1 can also be completely dielectric-coated at least on their facing sides facing the plasma.
- this has the advantage that the metallic surfaces are largely protected against corrosion.
- the distances b, c and d of the figure, which were defined above as the pitch, can also be different from one another. The stroke distance is thus varied, in particular in the reverse region of the exhaust gas flow, which can have advantages in practice. It is also possible for the cross section of the tubes to deviate from the circular shape and for example to be elliptical or also rectangular.
Abstract
In motor vehicles for example, exhaust fumes are to flow through a plasma reactor that works according to the principle of dielectrically inhibited discharge ('silent discharge'). The plasma reactor consists of at least two electrodes and at least one dielectric body. Known plasma reactors contain several adjacent discharge section. According to the invention, several concentric discharge sections (2 to 9) follow each other in the direction of flow, two pipe systems (10, 20) being coaxially nested into each other for that purpose. At least one pipe system (10, 20), preferably the second pipe system (20), is coated on its sides exposed to the exhaust fumes with a dielectric material.
Description
Beschreibungdescription
Vorrichtung zur Entgiftung von Abgasen aus mobilen AnlagenDevice for the detoxification of exhaust gases from mobile systems
Die Erfindung bezieht sich auf eine Vorrichtung zur Entgif¬ tung von Abgasen aus mobilen Anlagen, bei der das Abgas einen nach dem Prinzip der dielektrisch behinderten Entladung arbeitenden Plasmareaktor durchläuft, der aus einer Anordnung ebener Platten gebildet ist, bei denen metallische und dielektrische Schichten abwechseln, wodurch räumlich neben¬ einander angeordnete Entladungsstrecken gebildet sind.The invention relates to a device for the decontamination of exhaust gases from mobile systems, in which the exhaust gas passes through a plasma reactor which works according to the principle of dielectric barrier discharge and is formed from an arrangement of flat plates in which metallic and dielectric layers alternate, whereby discharge paths arranged spatially next to one another are formed.
Bei dielektrisch behinderten Entladungen spricht man auch von einer "stillen Entladung". Derartige stille Entladungen wer- den zwischen Elektroden erzeugt, zwischen denen sich minde¬ stens eine dielektrische Schicht oder ein dielektrischer Kör¬ per befindet und zwar derart, daß eine Gasentladung auf direktem Wege, d.h. von Elektrode zu Elektrode, nicht möglich ist.In the case of dielectrically disabled discharges, one also speaks of a "silent discharge". Such silent discharges are generated between electrodes, between which there is at least one dielectric layer or body, in such a way that a gas discharge is direct, i.e. from electrode to electrode, is not possible.
Vom Stand der Technik sind Vorrichtungen zur Erzeugung stil¬ ler Entladungen bekannt. Häufig werden derartige Vorrichtun¬ gen für Ozonisatoren verwendet und haben hier üblicherweise eine koaxiale Geometrie.Devices for generating stylish discharges are known from the prior art. Such devices are often used for ozonizers and usually have a coaxial geometry here.
Andere dem Stand der Technik entsprechende Vorrichtungen zur Erzeugung von stillen Entladungen besitzen planparallele An¬ ordnungen von Elektroden und dienen der Erzeugung von UV- Strahlung.Other devices corresponding to the prior art for generating silent discharges have plane-parallel arrangements of electrodes and are used to generate UV radiation.
Aus der DE-OS 37 08 508 ist bereits eine Einrichtung bekannt, die zum Vermindern von Schadstoffen in Verbrennungsabgasen dient, bei der im Abgaskanal mindestens ein Reaktionsraum an¬ geordnet ist, der aus metallischen, parallelen Platten oder konzentrischen Rohren gebildet ist und einen Spaltquerschnitt
hat, wobei mindestens eine Platte oder ein Rohr des Reaktionsraums mit einem elektrisch isolierenden dielektri¬ schen Material überzogen ist. Weiterhin ist aus der WO-A- 92/19361 eine derartige Vorrichtung bekannt, bei der ein Ab- gas in einen ringförmigen Raum zwischen einem äußeren Metali¬ zylinder und einem Innenzylinder aus Keramik geleitet wird.From DE-OS 37 08 508 a device is already known which serves to reduce pollutants in combustion exhaust gases, in which at least one reaction space is arranged in the exhaust gas duct, which is formed from metallic, parallel plates or concentric tubes and has a gap cross section has, wherein at least one plate or a tube of the reaction chamber is coated with an electrically insulating dielectric material. Furthermore, such a device is known from WO-A-92/19361, in which an exhaust gas is conducted into an annular space between an outer metal cylinder and an inner cylinder made of ceramic.
Bei vorstehendem Stand der Technik geht es insbesondere darum, das Verfahren zur Entgiftung von Abgasen nach dem Prinzip der dielektrisch behinderten Entladung in seiner Funktionsweise zu verdeutlichen. Es werden dort jeweils Kraftwerke einerseits und auch Kraftfahrzeuge andererseits angesprochen, wobei die konstruktive Ausbildung der Vorrich¬ tungen nicht genau spezifiziert ist.The prior art in particular is concerned with clarifying the functioning of the method for detoxifying exhaust gases according to the principle of dielectric barrier discharge. Power plants on the one hand and also motor vehicles on the other hand are addressed there, the construction of the devices not being specified precisely.
Insbesondere zur Verwendung bei mobilen Anlagen ist eine kom¬ pakte Bauweise des Plasmareaktors zwingend erforderlich. Gleichzeitig soll aber eine große wirksame Länge und/oder ein großer wirksamer Querschnitt des Reaktionsraums sicher- gestellt werden.A compact design of the plasma reactor is imperative, particularly for use in mobile systems. At the same time, however, a large effective length and / or a large effective cross section of the reaction space should be ensured.
Ausgehend von dem bekannten Plasmareaktor aus mehreren räum¬ lich nebeneinander angeordneten Entladungεstrecken ist es da¬ her Aufgabe der Erfindung, bei kompakter, raumsparender Bau- weise eine große wirksame Länge zu realisieren.Starting from the known plasma reactor comprising a plurality of discharge sections arranged spatially next to one another, it is therefore an object of the invention to achieve a large effective length with a compact, space-saving design.
Die Aufgabe ist erfindungsgemäß bei einer Vorrichtung der eingangs genannten Art dadurch gelöst, daß die Entladungs¬ strecken strömungsmäßig hintereinander geschaltet und konzen- trisch zueinander angeordnet sind, wozu zwei Rohrsysteme koaxial ineinandergeschachtelt sind. Vorzugsweise besteht da¬ bei das erste Rohrsystem aus wenigstens drei auf einer Trag¬ platte koaxial angeordneten metallischen Rohren und das zwei¬ te Rohrsystem aus wenigstens zwei auf einer Tragplatte koaxial angeordneten Rohren. Diese beiden Rohrsysteme sind zum Aufbau des Reaktors ineinandergeschachtelt.
Bei der Erfindung ist vorteilhafterweise das zweite Rohr- system, das keine äußere Wandung des Plasmareaktors bildet, auf der gesamten Oberfläche mit einer dielektrischen Schicht belegt . Es können aber auch beide Rohrsysteme an ihren dem Plasma zugewandten Seiten dielektrisch beschichtet sein.The object is achieved according to the invention in a device of the type mentioned at the outset in that the discharge sections are connected in series in terms of flow and are arranged concentrically to one another, for which purpose two tube systems are nested coaxially one inside the other. The first pipe system preferably consists of at least three metallic pipes arranged coaxially on a support plate and the second pipe system consists of at least two pipes arranged coaxially on a support plate. These two pipe systems are nested to build the reactor. In the invention, the second tube system, which does not form an outer wall of the plasma reactor, is advantageously covered with a dielectric layer on the entire surface. However, both pipe systems can also be dielectrically coated on their sides facing the plasma.
Weitere Einzelheiten und Vorteile der Erfindung ergeben sich aus der nachfolgenden Figurenbeschreibung von Ausführungsbei- spielen. Es zeigen dieFurther details and advantages of the invention result from the following figure description of exemplary embodiments. They show
Figur 1 einen Plasmareaktor in Schnittbilddarstellung, die Figuren 2 und 3 die beiden Rohrsysteme zum Aufbau desFigure 1 shows a plasma reactor in a sectional view, Figures 2 and 3, the two pipe systems to build the
Plasmareaktors gemäß Figur 1 und Figur 4 einen zur Figur 1 senkrechten Schnitt des Plasmareaktors.1 and FIG. 4 a section of the plasma reactor perpendicular to FIG. 1.
Die Figuren werden nachfolgend gemeinsam beschrieben.The figures are described together below.
In Figur 1 ist mit 1 ein Reaktor gekennzeichnet, der gemäß den Figuren 2 und 3 aus zwei Rohrsystemen 10 und 20 besteht, die koaxial ineinandergeschachtelt sind.In FIG. 1, 1 denotes a reactor which, according to FIGS. 2 and 3, consists of two pipe systems 10 and 20 which are nested coaxially one inside the other.
Das Rohrsystem 10 gemäß Figur 2 besteht beispielsweise aus drei auf einer kreisringförmigen Tragplatte 11 koaxial ange- ordneten metallischen Rohren 12, 13 und 14. Das innere Rohr 12 durchbricht die Tragplatte 11 und dient als Gaseinlaßrohr. Sein Durchmesser ist durch die Erfordernisse der abgaserzeu¬ genden Anlage gegeben. Innen- und Außendurchmesser der weite¬ ren Rohre 13 und 14 sind so gewählt, daß die radialen Abstän- de a der Rohre 11 bis 13 untereinander gleich sind und daß die Rohre 11 bis 13 des Rohrsystems 10 zu denjenigen des Rohrsystems 20 überall den gleichen Abstand s haben.The pipe system 10 according to FIG. 2 consists, for example, of three metallic pipes 12, 13 and 14 arranged coaxially on an annular support plate 11. The inner pipe 12 breaks through the support plate 11 and serves as a gas inlet pipe. Its diameter is determined by the requirements of the exhaust gas generating system. The inside and outside diameters of the further tubes 13 and 14 are selected such that the radial distances a between the tubes 11 to 13 are equal to one another and that the tubes 11 to 13 of the tube system 10 are the same distance from those of the tube system 20 everywhere have s.
In einer anderen Ausführungsform, die nicht im einzelnen dar- gestellt ist, können die Abstände der Rohre 11 bis 13 so ge¬ wählt werden, daß der zu durchströmende Querschnitt als Funk¬ tion des Abstandes R von der Mittelachse konstant bleibt,
d.h. d ~ R--*- ist. In einer weiteren Ausführungsform wird die Schlagweite der stillen Entladung gezielt als Funktion des Radius verändert .In another embodiment, which is not shown in detail, the distances between the tubes 11 to 13 can be selected such that the cross section to be flowed through remains constant as a function of the distance R from the central axis, ie d ~ R - * - is. In a further embodiment, the striking distance of the silent discharge is specifically changed as a function of the radius.
In der Figur 2 ist der Außendurchmesser des äußeren Rohrs 14 gleich dem Durchmesser der Tragplatte 11. Die Enden der inneren Rohre 12 und 13 haben den gleichen Abstand 1 von der Tragplatte 11. Das äußere Rohr 14 ragt soweit über die Rohre 12 und 13 hinaus, daß das Rohrsystem 20 in der aus dem Rohr- System 10 und einer Abschlußplatte 30 gebildeten Kammer 1 Platz findet. Dabei ist einerseits der Abstand b der Enden des Rohrεystems 20 zur Tragplatte 11, andererseits der Ab¬ stand c der Enden der Rohre 12 und 13 zur Tragplatte 21 des Rohrsystems 20 und weiterhin der Abstand d der Tragplatte 21 des Rohrsystems zur Abschlußplatte 30 gleich der Schlagweite, so daß gilt2, the outer diameter of the outer tube 14 is equal to the diameter of the support plate 11. The ends of the inner tubes 12 and 13 are at the same distance 1 from the support plate 11. The outer tube 14 extends beyond the tubes 12 and 13 so far, that the pipe system 20 takes place in the chamber 1 formed from the pipe system 10 and an end plate 30. On the one hand, the distance b between the ends of the pipe system 20 and the support plate 11, on the other hand, the distance c between the ends of the pipes 12 and 13 and the support plate 21 of the pipe system 20 and furthermore the distance d between the support plate 21 of the pipe system and the end plate 30 is equal to the lay length , so that applies
b = c = d = s.b = c = d = s.
Das Rohrsystem 20 gemäß Figur 3 besteht aus Metallteilen und ist auf seiner gesamten inneren und äußeren Oberfläche mit einer dielektrischen Schicht 28 belegt. Es besteht beispiels¬ weise aus zwei auf einer kreisringförmigen Tragplatte 21 koaxial angeordneten Rohren 22 und 23.The pipe system 20 according to FIG. 3 consists of metal parts and is covered on its entire inner and outer surface with a dielectric layer 28. It consists, for example, of two tubes 22 and 23 arranged coaxially on an annular support plate 21.
Innen- und Außendurchmesser der Rohre 21 und 22 sind in Figur 3 so gewählt, daß die radialen Abstände e der dielektrisch beschichteten Rohre untereinander gleich sind und daß die Rohre des Rohrsystems 20 zu denjenigen des Rohrsystems 10 überall den gleichen radialen Abstand s haben. Der Außen¬ durchmesser des äußeren Rohres 23 ist gleich dem Durchmesser der Tragplatte 21. Die Abstände m der Enden der Rohre 21 und 23 von der Tragplatte sind gleich. Das Rohrsystem 20 wird derart in das Rohrsystem eingebracht, daß die bei der Be- Schichtung des Rohrsystems 10 genannten Anforderungen an die Abstände erfüllt sind. Der radiale Abstand a der Rohre 14 und
23 wird durch elektrisch nic'it leitende Distanzstücke ge¬ wahrt.The inner and outer diameters of the tubes 21 and 22 are chosen in FIG. 3 such that the radial distances e of the dielectric coated tubes are the same among one another and that the tubes of the tube system 20 have the same radial distance s everywhere as those of the tube system 10. The outer diameter of the outer tube 23 is equal to the diameter of the support plate 21. The distances m of the ends of the tubes 21 and 23 from the support plate are the same. The pipe system 20 is introduced into the pipe system in such a way that the spacing requirements mentioned when coating the pipe system 10 are met. The radial distance a of the tubes 14 and 23 is electrically nic 'ge it conductive spacers respects.
Wie bereits erwähnt, können die Abstände der Rohre 21 und 23 so gewählt werden, daß der zu durchströmende Querschnitt als Funktion des Abstandeε von der Mittelachse entweder konstant bleibt oder daß die Schlagweite s unterschiedliche, besonders vorteilhafte Werte annimmt.As already mentioned, the distances between the tubes 21 and 23 can be selected so that the cross-section to be flowed through as a function of the distance from the central axis either remains constant or that the stroke length s assumes different, particularly advantageous values.
In Figur 3 ist die Tragplatte 21 an einer geeigneten Stelle mit einer Zuleitung 26 elektrisch leitend verbunden. Die Zu¬ leitung ist mit einer dielektrischen Schicht 28 ummantelt, die lückenlos an die dielektrische ßesc ichtung des Rohr¬ systems 20 anschließt und wird durch die Abschlußplatte 30 hindurch aus der Reaktionska-^mer hinausgeführt. Die Ab¬ schlußplatte 30 besitzt einei. Gasauslaßstutzen 31, dessen Durchmesser gleich dem Durchmesser des Gaseinlaßrohres 12 ist.In Figure 3, the support plate 21 is electrically conductively connected to a supply line 26 at a suitable point. The feed line is encased with a dielectric layer 28, which connects seamlessly to the dielectric sealing of the pipe system 20 and is led through the end plate 30 out of the reaction chamber. The end plate 30 has a. Gas outlet connection 31, the diameter of which is equal to the diameter of the gas inlet pipe 12.
Die Rohrsysteme 10 und 20 sind also Elektroden, zwischen denen eine stille Entladung betreibbar ist. Hierzu werden sie mit einem Generator 40 verbunden, der eine elektrische Span¬ nung mit geeignetem zeitlichen Verlauf, Amplitude, Frequenz und/oder Impulsform, Puls-/Pausenverhältnis zur Verfügung stellt. Der durch die Rohrsysteme gebildete Plasmareaktor wird in beliebiger, z.B. in der durch die Pfeile in Figur 1 angegebenen Richtung vom Abgas durchströmt.The pipe systems 10 and 20 are therefore electrodes between which a silent discharge can be operated. For this purpose, they are connected to a generator 40, which provides an electrical voltage with a suitable time profile, amplitude, frequency and / or pulse shape, pulse / pause ratio. The plasma reactor formed by the pipe systems is used in any, e.g. Flows through the exhaust gas in the direction indicated by the arrows in FIG. 1.
Die beispielhaft angegebene Anzahl der Rohre der Rohrsysteme 10 und 20 ist nicht auf drei bzw. zwei beschränkt. Sie ergibt sich, ebenso wie die Gesamtlänge der Anordnung, aus dem ge¬ wünschten Entgiftungsgrad und aus den Eingangsparametern. Das nicht mit einer dielektrischen Schicht versehene Rohrsystem kann zur Erzielung einer verbesserten Entgiftung an der dem Abgas zugewandten Seite mit einem herkömmlichen Katalysator¬ material belegt sein. Anstelle des Rohrsystems 20 kann auch das Rohrsystem 10 an der dem Abgas zugewandten Seite dielek-
trisch beschichtet sein. Insbesondere kann dazu ein kerami¬ sches Katalysatormaterial die Rolle des Dielektrikums über¬ nehmen. Ein solches Material kann beispielsweise aus Mischun¬ gen, die Titanoxid, Vanadiumoxid und Wolframoxid enthalten, bestehen.The number of pipes of the pipe systems 10 and 20 given by way of example is not limited to three or two. Like the total length of the arrangement, it results from the desired degree of detoxification and from the input parameters. The pipe system not provided with a dielectric layer can be coated with a conventional catalyst material on the side facing the exhaust gas in order to achieve improved detoxification. Instead of the pipe system 20, the pipe system 10 can also have a dielectric on the side facing the exhaust gas. be coated trically. In particular, a ceramic catalyst material can take on the role of the dielectric. Such a material can consist, for example, of mixtures containing titanium oxide, vanadium oxide and tungsten oxide.
Bei weiteren Ausführungsformen können auch beide Rohrsysteme 10 und 20 der Figur 1 mindestens an ihren dem Plasma zuge¬ wandten zugewandten Seiten komplett dielektrisch beschichtet sein. Außer der Entgiftungswirkung bietet dies den Vorteil, daß die metallischen Oberflächen gegen Korrosion weitgehend geschützt sind. Weiterhin können die Abstände b, c und d der Figur, die vorstehend gleich der Schlagweite definiert wur¬ den, auch voneinander verschieden sein. Damit wird die Schlagweite speziell im Umkehrbereich des AbgasStromes vari¬ iert, was Vorteile in der Praxis haben kann. Es ist auch mög¬ lich, daß der Querschnitt der Rohre von der Kreisform abwei¬ chen kann und beispielsweise elliptisch oder auch rechteckig ausgebildet ist.
In further embodiments, both pipe systems 10 and 20 of FIG. 1 can also be completely dielectric-coated at least on their facing sides facing the plasma. In addition to the detoxification effect, this has the advantage that the metallic surfaces are largely protected against corrosion. Furthermore, the distances b, c and d of the figure, which were defined above as the pitch, can also be different from one another. The stroke distance is thus varied, in particular in the reverse region of the exhaust gas flow, which can have advantages in practice. It is also possible for the cross section of the tubes to deviate from the circular shape and for example to be elliptical or also rectangular.
Claims
1. Vorrichtung zur Entgiftung von Abgasen aus mobilen Anla¬ gen, bei der das Abgas einen nach dem Prinzip der dielek- trisch behinderten Entladung arbeitenden Plasmareaktor durch¬ läuft, der eine Anordnung aus wenigstens zwei Elektroden und wenigstens einem dielektrischen Körper aufweist, wobei der Plasmareaktor aus mehreren räumlich nebeneinander angeordne¬ ten Entladungsstrecken besteht, d a d u r c h g e k e n n z e i c h n e t , daß die Entladungsstrecken (2 bis 9) strömungsmäßig hintereinandergeschaltet und konzen¬ trisch zueinander angeordnet ind, wozu zwei Rohrsysteme (10, 20) koaxial ineinander gescha htelc sind.1. Device for the detoxification of exhaust gases from mobile systems, in which the exhaust gas passes through a plasma reactor which works according to the principle of dielectric barrier discharge and which has an arrangement of at least two electrodes and at least one dielectric body, the plasma reactor Consists of several spatially arranged discharge paths, characterized in that the discharge paths (2 to 9) are connected in series in terms of flow and are arranged concentrically to one another, for which purpose two tube systems (10, 20) are coaxially interconnected.
2. Vorrichtung nach Anspruch 1, d a d u r c h g e ¬ k e n n z e i c h n e t , daß das erste Rohrsystem (10) aus wenigstens drei auf einer kreisringförmigen Tragplatte (11) koaxial angeordneten metallischen Rohren (12 bis 14) besteht.2. Device according to claim 1, so that the first pipe system (10) consists of at least three metallic pipes (12 to 14) coaxially arranged on an annular support plate (11).
3. Vorrichtung nach Anspruch 1, d a d u r c h g e ¬ k e n n z e i c h n e t , daß das zweite Rohrsystem (20) aus Metallteilen (21 bis 23) besteht, die auf der gesamten Oberfläche mit einer dielektrischen Schicht (28) belegt sind.3. Device according to claim 1, so that the second pipe system (20) consists of metal parts (21 to 23) which are covered with a dielectric layer (28) on the entire surface.
4. Vorrichtung nach Anspruch 3, d a d u r c h g e ¬ k e n n z e i c h n e t , daß das zweite Rohrsystem (20) aus wenigstens zwei auf einer kreisringförmigen Tragplatte .(21) koaxial angeordneten Rohren (22, 23) besteht.4. Apparatus according to claim 3, so that the second pipe system (20) consists of at least two pipes (22, 23) arranged coaxially on an annular support plate (21).
5. Vorrichtung nach Anspruch 3, d a d u r c h g e ¬ k e n n z e i c h n e t , daß beide Rohrsysteme (10, 20) mindestens an ihren dem Abgas zugewandten Seiten dielektrisch beschichtet sind5. The apparatus of claim 3, d a d u r c h g e ¬ k e n n z e i c h n e t that both pipe systems (10, 20) are dielectric coated at least on their sides facing the exhaust gas
6. Vorrichtung nach Anspruch 3 oder Anspruch 5, d a ¬ d u r c h g e k e n n z e i c h n e t , daß die dielek¬ trische Schicht aus keramischem Katalysatormaterial besteht, insbesondere aus Mischungen, die Titanoxid, Vanadiumoxid und Wolframoxid enthalten.6. Apparatus according to claim 3 or claim 5, since ¬ characterized in that the dielectric layer consists of ceramic catalyst material, in particular from mixtures containing titanium oxide, vanadium oxide and tungsten oxide.
7. Vorrichtung nach Anspruch 1, d a d u r c h g e - k e n n z e i c h n e t , daß die Schlagweite in den weiter außen liegenden Entladungsstrecken kleiner als die der inner¬ sten Entladungεstrecke ist. 7. The device as claimed in claim 1, so that the striking distance in the more distant discharge paths is smaller than that of the innermost discharge path.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEG9407861.0U | 1994-05-11 | ||
DE9407861U DE9407861U1 (en) | 1994-05-11 | 1994-05-11 | Device for the detoxification of exhaust gases from mobile systems |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1995031270A1 true WO1995031270A1 (en) | 1995-11-23 |
Family
ID=6908560
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/DE1995/000618 WO1995031270A1 (en) | 1994-05-11 | 1995-05-10 | Device for detoxifying exhaust fumes from mobile equipments |
Country Status (2)
Country | Link |
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DE (1) | DE9407861U1 (en) |
WO (1) | WO1995031270A1 (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1999043419A1 (en) * | 1998-02-25 | 1999-09-02 | Aea Technology Plc | A component for gas treatment |
GB2346528A (en) * | 1999-01-21 | 2000-08-09 | Aea Technology Plc | Power supply for processing of gaseous media |
EP1047503A1 (en) * | 1997-11-25 | 2000-11-02 | State Of Israel Ministry Of Defence Rafael Armament Development Authority | Modular dielectric barrier discharge device for pollution abatement |
KR100397169B1 (en) * | 2001-02-06 | 2003-09-06 | 선도전기주식회사 | exhaust-gas treatment apparatus |
US6685803B2 (en) | 2001-06-22 | 2004-02-03 | Applied Materials, Inc. | Plasma treatment of processing gases |
CN113356966A (en) * | 2021-06-17 | 2021-09-07 | 东风小康汽车有限公司重庆分公司 | Automobile exhaust particle processor and exhaust treatment device |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
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US5914015A (en) * | 1996-07-15 | 1999-06-22 | Battelle Memorial Institute | Method and apparatus for processing exhaust gas with corona discharge |
GB9911728D0 (en) * | 1999-05-21 | 1999-07-21 | Aea Technology Plc | Dielectric barrier gas reactors with non-axial flow |
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Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
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EP1047503A1 (en) * | 1997-11-25 | 2000-11-02 | State Of Israel Ministry Of Defence Rafael Armament Development Authority | Modular dielectric barrier discharge device for pollution abatement |
EP1047503A4 (en) * | 1997-11-25 | 2002-04-17 | Rafael Armament Dev Authority | Modular dielectric barrier discharge device for pollution abatement |
WO1999043419A1 (en) * | 1998-02-25 | 1999-09-02 | Aea Technology Plc | A component for gas treatment |
GB2346528A (en) * | 1999-01-21 | 2000-08-09 | Aea Technology Plc | Power supply for processing of gaseous media |
KR100397169B1 (en) * | 2001-02-06 | 2003-09-06 | 선도전기주식회사 | exhaust-gas treatment apparatus |
US6685803B2 (en) | 2001-06-22 | 2004-02-03 | Applied Materials, Inc. | Plasma treatment of processing gases |
CN113356966A (en) * | 2021-06-17 | 2021-09-07 | 东风小康汽车有限公司重庆分公司 | Automobile exhaust particle processor and exhaust treatment device |
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