DE4141580A1 - Exhaust gas particle filter esp. for diesel exhaust - has at least two filter layers of different ceramics between the clean and crude gas sides, the first filter being coarser than the second, giving high sepn. and low pressure loss - Google Patents
Exhaust gas particle filter esp. for diesel exhaust - has at least two filter layers of different ceramics between the clean and crude gas sides, the first filter being coarser than the second, giving high sepn. and low pressure lossInfo
- Publication number
- DE4141580A1 DE4141580A1 DE4141580A DE4141580A DE4141580A1 DE 4141580 A1 DE4141580 A1 DE 4141580A1 DE 4141580 A DE4141580 A DE 4141580A DE 4141580 A DE4141580 A DE 4141580A DE 4141580 A1 DE4141580 A1 DE 4141580A1
- Authority
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- Germany
- Prior art keywords
- filter
- gas side
- clean gas
- ceramic
- porosity
- Prior art date
- 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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Classifications
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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
- F01N3/02—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
- F01N3/021—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters
- F01N3/022—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters characterised by specially adapted filtering structure, e.g. honeycomb, mesh or fibrous
- F01N3/0226—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters characterised by specially adapted filtering structure, e.g. honeycomb, mesh or fibrous the structure being fibrous
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/14—Other self-supporting filtering material ; Other filtering material
- B01D39/20—Other self-supporting filtering material ; Other filtering material of inorganic material, e.g. asbestos paper, metallic filtering material of non-woven wires
- B01D39/2068—Other inorganic materials, e.g. ceramics
- B01D39/2082—Other inorganic materials, e.g. ceramics the material being filamentary or fibrous
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/24—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/56—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition
- B01D46/62—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition connected in series
- B01D46/64—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition connected in series arranged concentrically or coaxially
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B18/00—Layered products essentially comprising ceramics, e.g. refractory products
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- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B38/00—Porous mortars, concrete, artificial stone or ceramic ware; Preparation thereof
- C04B38/007—Porous mortars, concrete, artificial stone or ceramic ware; Preparation thereof characterised by the pore distribution, e.g. inhomogeneous distribution of pores
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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
- F01N3/02—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
- F01N3/021—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters
- F01N3/0217—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters the filtering elements having the form of hollow cylindrical bodies
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
- B01D2239/06—Filter cloth, e.g. knitted, woven non-woven; self-supported material
- B01D2239/065—More than one layer present in the filtering material
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
- B01D2239/06—Filter cloth, e.g. knitted, woven non-woven; self-supported material
- B01D2239/065—More than one layer present in the filtering material
- B01D2239/0654—Support layers
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
- B01D2239/06—Filter cloth, e.g. knitted, woven non-woven; self-supported material
- B01D2239/069—Special geometry of layers
- B01D2239/0695—Wound layers
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2275/00—Filter media structures for filters specially adapted for separating dispersed particles from gases or vapours
- B01D2275/20—Shape of filtering material
- B01D2275/206—Special forms, e.g. adapted to a certain housing
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- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2111/00—Mortars, concrete or artificial stone or mixtures to prepare them, characterised by specific function, property or use
- C04B2111/00474—Uses not provided for elsewhere in C04B2111/00
- C04B2111/00793—Uses not provided for elsewhere in C04B2111/00 as filters or diaphragms
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- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2237/00—Aspects relating to ceramic laminates or to joining of ceramic articles with other articles by heating
- C04B2237/30—Composition of layers of ceramic laminates or of ceramic or metallic articles to be joined by heating, e.g. Si substrates
- C04B2237/32—Ceramic
- C04B2237/34—Oxidic
- C04B2237/341—Silica or silicates
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- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2237/00—Aspects relating to ceramic laminates or to joining of ceramic articles with other articles by heating
- C04B2237/30—Composition of layers of ceramic laminates or of ceramic or metallic articles to be joined by heating, e.g. Si substrates
- C04B2237/32—Ceramic
- C04B2237/34—Oxidic
- C04B2237/343—Alumina or aluminates
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- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2237/00—Aspects relating to ceramic laminates or to joining of ceramic articles with other articles by heating
- C04B2237/50—Processing aspects relating to ceramic laminates or to the joining of ceramic articles with other articles by heating
- C04B2237/84—Joining of a first substrate with a second substrate at least partially inside the first substrate, where the bonding area is at the inside of the first substrate, e.g. one tube inside another tube
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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
- F01N2330/00—Structure of catalyst support or particle filter
- F01N2330/06—Ceramic, e.g. monoliths
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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
- F01N2330/00—Structure of catalyst support or particle filter
- F01N2330/10—Fibrous material, e.g. mineral or metallic wool
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02B—INTERNAL-COMBUSTION PISTON ENGINES; COMBUSTION ENGINES IN GENERAL
- F02B3/00—Engines characterised by air compression and subsequent fuel addition
- F02B3/06—Engines characterised by air compression and subsequent fuel addition with compression ignition
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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
- 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
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Ceramic Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Combustion & Propulsion (AREA)
- General Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Structural Engineering (AREA)
- Inorganic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Filtering Materials (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
- Processes For Solid Components From Exhaust (AREA)
Abstract
Description
Die Erfindung betrifft ein Partikelfilter zur Reinigung von Abgasen, insbesondere zur Reinigung von Dieselabgasen, mit keramischem Filtermaterial zwischen der Rohgasseite und der Reingasseite.The invention relates to a particle filter for cleaning Exhaust gases, especially for cleaning diesel exhaust gases, with ceramic filter material between the raw gas side and the Clean gas side.
Für die Rußpartikelfiltration werden verschiedene Typen von Filtermaterialien verwendet. Dabei ist jedoch zwischen der Rohgasseite und der Reingasseite eines jeweiligen Partikelfilters nach dem Stand der Technik nur das gleiche Filtermaterial eingesetzt.Different types of are used for soot particle filtration Filter materials used. However, it is between the Raw gas side and the clean gas side of a respective Particle filter according to the prior art only the same Filter material used.
Es ist bekannt, als Filtermaterial Cordierit als Monolith zu verwenden. Dabei steht für die Ablagerung der Rußpartikel eine grobe innere Oberfläche zur Verfügung. Die durchgängige Porosität ist gering. Sie liegt unter 5%. Der mittlere Durchmesser der durchgängigen Poren ist kleiner als 50 µm. Der Abscheidegrad ist hoch und liegt bei etwa 97%. Der Druckverlustgradient ist klein. Das Filter braucht nur alle vier bis fünf Stunden regeneriert zu werden. Das Filtermaterial ist allerdings empfindlich gegen thermische Spannungen, die vor allem beim Regenerieren des Filters auftreten. Reibt das Filtermaterial, dann sinkt der Abscheidegrad schnell unter 60% ab. It is known to use cordierite as a monolith as a filter material use. It stands for the deposition of the soot particles a rough inner surface is available. The end-to-end Porosity is low. It is below 5%. The middle one The diameter of the continuous pores is less than 50 µm. The degree of separation is high and is around 97%. The Pressure drop gradient is small. The filter only needs everyone to be regenerated for four to five hours. The However, filter material is sensitive to thermal Voltages especially when regenerating the filter occur. If the filter material rubs, it sinks Degree of separation quickly drops below 60%.
Weiterhin wird nach dem Stand der Technik ein Filtermaterial aus keramischen Fasern verwendet. Ein solches Filtermaterial hat eine sehr grobe durchgängige Porosität und eine grobe innere Oberfläche. Große Partikel werden sicher ausgefiltert. Kleinere Partikel dagegen können auf die Reingasseite gelangen. Es werden hier Abscheidegrade von etwa 70% erreicht. Ein solches Filtermaterial arbeitet als Tiefenfilter.Furthermore, a filter material according to the prior art made of ceramic fibers. Such a filter material has a very coarse and continuous porosity inner surface. Large particles become safe filtered out. Smaller particles, on the other hand, can affect the Get clean gas side. Separation levels of reached about 70%. Such a filter material works as Depth filter.
Außerdem werden Filter aus Poröskeramik in Betracht gezogen. Diese können wie Tiefenfilter wirken, wenn der Durchmesser der durchgängigen Poren ausreichend grob eingestellt wird. Bei mittleren Porendurchmessern unter 100 µm bildet der Ruf auf der Oberfläche des Filtermaterials, speziell an der Rohgasseite, Brücken aus Rußpartikeln. Diese unterstützen die Filterwirkung. Mit solchen Oberflächenfiltern sind Abscheidegrade von nahezu 100% zu erreichen. Allerdings führt die rohgasseitige Brückenbildung zu einer Verstopfung der Poreneingänge. Infolge der sich aufbauenden Rußschicht steigt der Druckverlust im Filtermaterial schnell an, so daß die Intervalle, nach denen das Filtermaterial regeneriert werden muß, kurz sind.Porous ceramic filters are also considered. These can act like depth filters if the diameter of the continuous pores is set sufficiently rough. With average pore diameters of less than 100 µm, the call forms on the surface of the filter material, especially on the Raw gas side, bridges made of soot particles. Support them the filter effect. With such surface filters Achieve separation rates of almost 100%. Indeed the bridging on the raw gas side leads to blockage of the pore entrances. As a result of the soot layer building up the pressure loss in the filter material increases rapidly, so that the intervals after which the filter material regenerates must be short.
In der Patentanmeldung P 40 32 086.3 ist ein Rußpartikelfilter aus Poröskeramik beschrieben.In patent application P 40 32 086.3 there is a Soot particle filter made of porous ceramic described.
In der DE 35 37 976 C1 ist ein Rußpartikelfilter beschrieben, bei dem keramische Platten, vorzugsweise aus keramischen Fasern, verwendet sind.DE 35 37 976 C1 is a soot particle filter described, in the ceramic plates, preferably made of ceramic fibers are used.
In der EP 03 20 458 A1 ist ein Rußpartikelfilter aus Cordierit-Schaumkeramik angegeben. In EP 03 20 458 A1, a soot particle filter is made Cordierite foam ceramic specified.
In der Firmenschrift "Auto und Umwelt", Daimler-Benz AG, Mai 1985, Seiten 24 bis 28 sind monolithische, keramische Filter und Wickelfilter aus Keramikgarn dargestellt. Letzteres ist in der DE 30 07 642 näher beschrieben.In the company brochure "Auto und Umwelt", Daimler-Benz AG, May 1985, pages 24 to 28 are monolithic, ceramic Filters and wound filters made of ceramic yarn are shown. The latter is described in more detail in DE 30 07 642.
Neben den keramischen Filtern sind auch metallische Filter bekannt. Solche sind in der DE-OS 19 53 304, der AT-PS 2 23 436, in der EP 03 31 885 B1 und in der EP 04 10 200 A1 beschrieben. Bei solchen Filtern lädt sich die Wirkung eines Oberflächenfilters nicht erreichen. Es handelt um Tiefenfilter.In addition to the ceramic filters, there are also metallic filters known. Such are in DE-OS 19 53 304, AT-PS 2 23 436, in EP 03 31 885 B1 and in EP 04 10 200 A1 described. With such filters, the effect of a Do not reach the surface filter. It's about Depth filter.
Aufgabe der Erfindung ist es, bei einem Partikelfilter der eingangs genannten Art einen hohen Abscheidegrad der Partikel bei geringem Druckverlustanstieg im Filter zu erreichen.The object of the invention is in a particulate filter a high degree of separation of the type mentioned Particles with little increase in pressure loss in the filter to reach.
Erfindungsgemäß ist obige Aufgabe bei einem Partikelfilter der eingangs genannten Art dadurch gelöst, daß zwischen der Rohgasseite und der Reingasseite wenigstens zwei Filterschichten aus unterschiedlichen keramischen Filtermaterialien angeordnet sind und daß das der Rohgasseite jeweils nähere erste Filtermaterial eine größere durchlässige Porosität aufweist als das der Reingasseite nähere andere Filtermaterial.According to the invention, the above task is for a particle filter of the type mentioned in that between the Raw gas side and the clean gas side at least two Filter layers made of different ceramic Filter materials are arranged and that the Raw gas side each closer to a larger filter material porous porosity than that of the clean gas side other filter material.
Das der Rohgasseite nahe Filtermaterial nimmt als Tiefenfilter einen groben Teil der Partikel, insbesondere die größeren Partikel auf. Das andere Filtermaterial nimmt als Oberflächenfilter die kleineren Partikel auf. Durch das Tiefenfilter ist die auf das Oberflächenfilter wirkende Rußmenge erheblich verkleinert. Dadurch führt die Rußablagerung auf dem Oberflächenfilter nur noch zu einem kleinen Druckverlustanstieg. Es ergibt sich daraus, daß der Filter insgesamt nur einen Druckverlustgradienten aufweist, der in der Größenordnung eines Filters liegt, der insgesamt aus Fasermaterial als Tiefenfilter aufgebaut ist. Durch die Erfindung ist also erreicht, daß einerseits grobe und kleine Partikel abgeschieden werden und daß andererseits im Filtersystem ein geringerer Druckverlustanstieg entsteht, als beim reinen Oberflächenfilter.The filter material close to the raw gas side takes as Depth filter a large part of the particles, in particular the larger particles. The other filter material takes the smaller particles as a surface filter. By the Depth filter is the one that acts on the surface filter Soot amount significantly reduced. This leads the Soot deposits on the surface filter only one small increase in pressure loss. It follows that the Filter has only a pressure drop gradient overall, which is on the order of a filter, the total is constructed from fiber material as a depth filter. Through the Invention is thus achieved that on the one hand coarse and small Particles are separated and that on the other hand in Filter system there is a lower increase in pressure loss, than with the pure surface filter.
Die als Oberflächenfilter wirkende Filterschicht, die insbesondere aus Poröskeramik besteht, filtert noch feinste Rußpartikel dadurch, daß der auf ihrer Oberfläche abgeschiedene Ruß selbst filternd wirkt. Im Zuge der Beladung mit Ruß nähert sich der Ruß-Abscheidegrad schnell 100%.The filter layer acting as a surface filter, the consists especially of porous ceramics, filters even the finest Soot particles in that the deposited on their surface Soot filters itself. In the course of loading with soot the degree of soot separation quickly approaches 100%.
Vorteilhafte Ausgestaltungen der Erfindung ergeben sich aus den Unteransprüchen und der folgenden Beschreibung von Ausführungsbeispielen. In der Zeichnung zeigtAdvantageous refinements of the invention result from the dependent claims and the following description of Embodiments. In the drawing shows
Fig. 1 einen Querschnitt einer Keramik-Filterkerze und Fig. 1 shows a cross section of a ceramic filter cartridge and
Fig. 2 einen Querschnitt eines Keramikfilters mit mehreren Filterkerzen. Fig. 2 shows a cross section of a ceramic filter with several filter cartridges.
Die Keramik-Filterkerze nach Fig. 1 besteht aus drei zylindrischen Filterschichten 1, 2, 3, die hintereinander zwischen der Rohgasseite 4 und der Reingasseite 5 angeordnet sind.The ceramic filter candle according to Fig. 1 consists of three cylindrical filter layers 1, 2, 3, one behind the other between the raw gas 4 and the clean gas side 5 are arranged.
Die rohgasseitige Filterschicht 3 und die an sie innen anschließende Filterschicht 2 bestehen aus einem keramischen Fasermaterial. The raw gas-side filter layer 3 and the filter layer 2 adjoining it on the inside consist of a ceramic fiber material.
Als keramisches Fasermaterial nach der vorliegenden Erfindung sind zu verstehen, beispielsweise Fasern mit mehr als 95% Al2O3 wie "Saffil" der Fa. ICI, sogenannte Fasern "1260" bzw. "1400" mit 47 bis 60% Al2O3 und 40 bis 53% SiO2 wie z. B. "Fibrefrax" der Fa. Carborundum, aber auch sogenannte Alumoborosilikatglas-Fasern, wie "Nextel" der Fa. 3M, oder temperaturbeständige glasige- oder Glasfasern und Fasern auf Basis "Silica" mit 99% SiO2.Ceramic fiber material according to the present invention is to be understood as, for example, fibers with more than 95% Al 2 O 3 such as "Saffil" from ICI, so-called fibers "1260" or "1400" with 47 to 60% Al 2 O 3 and 40 to 53% SiO 2 such as. B. "Fibrefrax" from Carborundum, but also so-called aluminum borosilicate glass fibers, such as "Nextel" from 3M, or temperature-resistant glassy or glass fibers and fibers based on "silica" with 99% SiO 2 .
Sie weisen eine hohe durchgängige, offene Porosität von 70% bis 98% mit grober innerer Oberfläche von beispielsweise 50000 m2/m3 auf. Die Filterschichten 2, 3 bestehen aus Matten, Blankets oder gewickelten Schnüren. Das die Filterschichten 2, 3 bildende Fasermaterial kann auch durch Spritzen oder mittels Vacuumsaugen auf die Filterschicht 1 aufgebracht sein.They have a high, continuous, open porosity of 70% to 98% with a coarse inner surface of, for example, 50,000 m 2 / m 3 . The filter layers 2 , 3 consist of mats, blankets or wound cords. The fiber material forming the filter layers 2 , 3 can also be applied to the filter layer 1 by spraying or by means of vacuum suction.
Die durchgängige Porosität der der Rohgasseite 4 entfernteren Filterschicht 2 ist kleiner gewählt als die Porosität der rohgasseitigen Filterschicht 3. Dadurch scheiden sich an der Filterschicht 2 solche, mittelgroßen Partikel ab, die durch die Filterschicht 3 hindurchgehen.The continuous porosity of the filter layer 2 further away from the raw gas side 4 is chosen to be smaller than the porosity of the filter layer 3 on the raw gas side. As a result, such medium-sized particles are deposited on the filter layer 2 and pass through the filter layer 3 .
Die reingasseitige Filterschicht 1 besteht aus einem Formkörper aus Poröskeramik. Solche Poröskeramik ist unter dem Handelsnamen Pantel der Anmelderin marktbekannt. Die Filterschicht 1 weist eine offene Porosität von etwa 35% bis 45% auf. Der mittlere Porendurchmesser der Filterschicht 1 ist wesentlich kleiner als der mittlere "Porendurchmesser" der angrenzenden Filterschicht 2. Der mittlere Porendurchmesser der Filterschicht 1 beträgt weniger als 10% des mittleren "Porendurchmessers" der Filterschicht 2. Die Filterschicht (1) wirkt im Gegensatz zu den Filterschichten 2, 3 als Oberflächenfilter. The clean gas side filter layer 1 consists of a molded body made of porous ceramic. Such porous ceramics are known on the market under the trade name Pantel by the applicant. The filter layer 1 has an open porosity of approximately 35% to 45%. The average pore diameter of the filter layer 1 is significantly smaller than the average "pore diameter" of the adjacent filter layer 2 . The average pore diameter of the filter layer 1 is less than 10% of the average "pore diameter" of the filter layer 2 . In contrast to the filter layers 2 , 3, the filter layer ( 1 ) acts as a surface filter.
Die Bezeichnung "Porendurchmesser" im Zusammenhang mit Faserwerkstoffen ist zumindest unpräzise, da das aus den Einzelfasern aufgebaute Gerüst keine Poren in herkömmlichem Sinne ausbildet.The term "pore diameter" related to Fiber materials is at least imprecise, because that is from the Single-fiber structure, no pores in conventional Trains the senses.
Die Funktionsweise der Filterkerze nach Fig. 1 ist etwa folgende:The functioning of the filter candle according to FIG. 1 is approximately as follows:
Mit Rußpartikeln beladene Dieselabgase gelangen zunächst in die sehr durchlässige Faser-Filterschicht 3, wobei sich in dieser die größeren Filterpartikel ablagern und dann in die zwar weniger, jedoch ebenfalls noch sehr durchlässige Faser-Filterschicht 2, in der sich weitere größere bzw. Mittelgröße Filterpartikel ablagern. Größere und mittlere Rußpartikel gelangen damit kaum auf die Oberfläche 6 der Filterschicht 1, so daß sie diese auch nicht verstopfen können. Die Filterschichten 2, 3 arbeiten also als Tiefenfilter und bilden nur einen geringen Strömungswiderstand, so daß sie auch im partikelbeladenen Zustand zu einem geringen Druckverlustanstieg führen.Diesel exhaust gases loaded with soot particles first enter the very permeable fiber filter layer 3 , in which the larger filter particles are deposited and then in the less, but also still very permeable fiber filter layer 2 , in which further larger or medium-sized filter particles are deposited . Larger and medium soot particles hardly reach the surface 6 of the filter layer 1 so that they cannot clog them. The filter layers 2 , 3 thus work as depth filters and form only a low flow resistance, so that they lead to a slight increase in pressure loss even in the particle-laden state.
An den Poren der Oberfläche 6 der Filterschicht 1 lagern sich nur noch kleinere Rußpartikel an. Diese verengen die Poreneingänge an der Filterschicht 1, was an sich die Filterwirkung unterstützt, so daß auch noch feinste Rußpartikel abgeschieden werden. Die Filterschicht 1 wirkt also als Oberflächenfilter. Somit wird im Endergebnis eine praktisch hundertprozentige Rußabscheidung erreicht. Da die Oberfläche 6 nicht schon durch größere Rußpartikel verstopft wird, steigt auch der auf der Filterschicht 1 beruhende Druckverlust im Laufe des Filterbetriebs nur gering an, so daß sich die Intervalle der Abreinigung der Filterschichten wesentlich verlängern. Es hat sich gezeigt, daß die Abreinigungsintervalle nicht größer sind, als bei einem Faserfilter bzw. Tiefenfilter ohne Oberflächenfilter.Only smaller soot particles are deposited on the pores of the surface 6 of the filter layer 1 . These narrow the pore inlets on the filter layer 1 , which in itself supports the filter effect, so that even the finest soot particles are separated. The filter layer 1 thus acts as a surface filter. The result is a practically one hundred percent soot separation. Since the surface 6 is not already clogged by larger soot particles, the pressure loss based on the filter layer 1 also increases only slightly during the course of the filter operation, so that the intervals for cleaning the filter layers are considerably extended. It has been shown that the cleaning intervals are not longer than in the case of a fiber filter or depth filter without a surface filter.
Bei dem Ausführungsbeispiel nach Fig. 2 ist in einem Gehäuse 7 eine Vielzahl von Filterkerzen 8 verteilt angeordnet. Die Filterkerzen 8 sind aus einer Poröskeramik, wie die anhand von Fig. 1 beschriebene Filterschicht 1.In the exemplary embodiment according to FIG. 2, a multiplicity of filter candles 8 are arranged in a housing 7 . The filter candles 8 are made of a porous ceramic, such as the filter layer 1 described with reference to FIG. 1 .
Der gesamte Raum außerhalb der Filterkerzen 8 und innerhalb des Gehäuses 7 ist mit einer Filterschicht 9 gefüllt. Diese besteht, wie bei den Filterschichten 2, 3 nach Fig. 1 beschrieben, aus einem keramischen Fasermaterial.The entire space outside the filter candles 8 and inside the housing 7 is filled with a filter layer 9 . As described for the filter layers 2 , 3 according to FIG. 1, this consists of a ceramic fiber material.
Die Funktionsweise des Filters nach Fig. 2 entspricht im wesentlichen der anhand von Fig. 1 beschriebenen Funktionsweise.The mode of operation of the filter according to FIG. 2 essentially corresponds to the mode of operation described with reference to FIG. 1.
Die Filterschicht 9 wirkt als Tiefenfilter mit grober durchlässiger Porosität und grober innerer Oberfläche, so daß sie vor allem größere Rußpartikel von den Oberflächen 6 der Filterkerzen 8 fernhält und kaum zu einem Druckverlust führt. An den als Oberflächenfilter wirkenden Filterkerzen 8 lagern sich dann nur noch kleinere Rußpartikel an, wobei kleinste Rußpartikel in den Filterkerzen 8 zurückgehalten werden.The filter layer 9 acts as a depth filter with a coarse permeable porosity and a coarse inner surface, so that it mainly keeps larger soot particles away from the surfaces 6 of the filter cartridges 8 and hardly leads to a loss of pressure. Only small soot particles are then deposited itself on the surface acts as a filter cartridges 8, wherein the smallest soot particles are retained in the filter cartridges. 8
Bei dem beschrieben Partikelfilter ist auch günstig, daß sich die Filterschichten 1, 2, 3 bzw. 8, 9 gegenseitig stützen. Dadurch wird die mechanische Stabilität und auch die Temperaturwechselbeständigkeit verbessert.In the particle filter described it is also favorable that the filter layers 1 , 2 , 3 and 8 , 9 support each other. This improves the mechanical stability and the resistance to temperature changes.
Claims (13)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE4141580A DE4141580A1 (en) | 1991-12-17 | 1991-12-17 | Exhaust gas particle filter esp. for diesel exhaust - has at least two filter layers of different ceramics between the clean and crude gas sides, the first filter being coarser than the second, giving high sepn. and low pressure loss |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE4141580A DE4141580A1 (en) | 1991-12-17 | 1991-12-17 | Exhaust gas particle filter esp. for diesel exhaust - has at least two filter layers of different ceramics between the clean and crude gas sides, the first filter being coarser than the second, giving high sepn. and low pressure loss |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| DE4141580A1 true DE4141580A1 (en) | 1993-06-24 |
Family
ID=6447239
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DE4141580A Withdrawn DE4141580A1 (en) | 1991-12-17 | 1991-12-17 | Exhaust gas particle filter esp. for diesel exhaust - has at least two filter layers of different ceramics between the clean and crude gas sides, the first filter being coarser than the second, giving high sepn. and low pressure loss |
Country Status (1)
| Country | Link |
|---|---|
| DE (1) | DE4141580A1 (en) |
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0679425A1 (en) * | 1994-04-25 | 1995-11-02 | INDUSTRIAL FILTER & PUMP MFG.CO. | Filter element and method of manufacture |
| DE19522312A1 (en) * | 1994-06-21 | 1996-01-04 | Ngk Insulators Ltd | Exhaust gas filter for esp. diesel engine of vehicle |
| WO1996041672A1 (en) * | 1995-06-09 | 1996-12-27 | Du Pont Lanxide Composites L.P. | Ceramic hot-gas filter and process for manufacturing it |
| DE19611150A1 (en) * | 1996-03-21 | 1997-05-28 | Mtu Friedrichshafen Gmbh | Particle filter for internal combustion engine |
| WO1998002231A1 (en) * | 1996-07-17 | 1998-01-22 | Minnesota Mining And Manufacturing Company | Filter material |
| US5849375A (en) * | 1996-07-17 | 1998-12-15 | Minnesota Mining & Manufacturing Company | Candle filter |
| WO1999033567A1 (en) * | 1997-12-24 | 1999-07-08 | Shell Internationale Research Maatschappij B.V. | Multiple layer monolithic structure and use thereof |
| EP0900922A3 (en) * | 1995-05-30 | 2000-06-28 | Sumitomo Electric Industries, Ltd. | Particulate trap for diesel engine |
| EP0957241A3 (en) * | 1998-05-14 | 2003-07-23 | Sumitomo Electric Industries, Ltd. | Particulate trap for diesel engine |
| WO2003103800A3 (en) * | 2002-06-05 | 2004-05-27 | Pall Corp | FILTER CARTRIDGE AND PROCESS FOR PRODUCING THE SAME |
| WO2004104386A3 (en) * | 2003-05-23 | 2005-01-06 | Bekaert Sa Nv | Diesel soot particulate filter medium |
| WO2006072606A3 (en) * | 2005-01-07 | 2006-08-31 | Emitec Emissionstechnologie | Method for eliminating particles contained in exhaust gases, fibrous layer and particulate filter |
| WO2007079829A1 (en) * | 2006-01-09 | 2007-07-19 | Nv Bekaert Sa | A diesel soot particulate filter medium |
| CN101384799B (en) * | 2006-02-20 | 2012-06-20 | 淡水河谷英可公司 | An apparatus for the separation of particles contained in exhaust gases of internal combustion engines |
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1991
- 1991-12-17 DE DE4141580A patent/DE4141580A1/en not_active Withdrawn
Cited By (22)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5500029A (en) * | 1994-04-25 | 1996-03-19 | Industrial Filter & Pump Mfg. Co. | Filter element and method of manufacture |
| EP0679425A1 (en) * | 1994-04-25 | 1995-11-02 | INDUSTRIAL FILTER & PUMP MFG.CO. | Filter element and method of manufacture |
| DE19522312A1 (en) * | 1994-06-21 | 1996-01-04 | Ngk Insulators Ltd | Exhaust gas filter for esp. diesel engine of vehicle |
| DE19522312C2 (en) * | 1994-06-21 | 1998-07-09 | Ngk Insulators Ltd | Exhaust filter and device for treating exhaust gases |
| EP0900922A3 (en) * | 1995-05-30 | 2000-06-28 | Sumitomo Electric Industries, Ltd. | Particulate trap for diesel engine |
| WO1996041672A1 (en) * | 1995-06-09 | 1996-12-27 | Du Pont Lanxide Composites L.P. | Ceramic hot-gas filter and process for manufacturing it |
| DE19611150A1 (en) * | 1996-03-21 | 1997-05-28 | Mtu Friedrichshafen Gmbh | Particle filter for internal combustion engine |
| WO1998002231A1 (en) * | 1996-07-17 | 1998-01-22 | Minnesota Mining And Manufacturing Company | Filter material |
| US5849375A (en) * | 1996-07-17 | 1998-12-15 | Minnesota Mining & Manufacturing Company | Candle filter |
| US5780126A (en) * | 1996-07-17 | 1998-07-14 | Minnesota Mining & Manufacturing | Filter material |
| WO1999033567A1 (en) * | 1997-12-24 | 1999-07-08 | Shell Internationale Research Maatschappij B.V. | Multiple layer monolithic structure and use thereof |
| EP0957241A3 (en) * | 1998-05-14 | 2003-07-23 | Sumitomo Electric Industries, Ltd. | Particulate trap for diesel engine |
| WO2003103800A3 (en) * | 2002-06-05 | 2004-05-27 | Pall Corp | FILTER CARTRIDGE AND PROCESS FOR PRODUCING THE SAME |
| WO2005040572A1 (en) * | 2003-05-23 | 2005-05-06 | N.V. Bekaert S.A. | Diesel soot particulate filter medium |
| WO2004104386A3 (en) * | 2003-05-23 | 2005-01-06 | Bekaert Sa Nv | Diesel soot particulate filter medium |
| CN100478548C (en) * | 2003-05-23 | 2009-04-15 | 贝卡尔特股份有限公司 | Diesel soot particulate filter medium |
| US7846230B2 (en) | 2003-05-23 | 2010-12-07 | Nv Bekaert Sa | Diesel soot particulate filter medium |
| WO2006072606A3 (en) * | 2005-01-07 | 2006-08-31 | Emitec Emissionstechnologie | Method for eliminating particles contained in exhaust gases, fibrous layer and particulate filter |
| US8012244B2 (en) | 2005-01-07 | 2011-09-06 | Emitec Gesellschaft Fuer Emissionstechnologie Mbh | Method of removing particulates from exhaust gases, and corresponding fiber layer, particulate filter, exhaust system and vehicle |
| WO2007079829A1 (en) * | 2006-01-09 | 2007-07-19 | Nv Bekaert Sa | A diesel soot particulate filter medium |
| CN101384799B (en) * | 2006-02-20 | 2012-06-20 | 淡水河谷英可公司 | An apparatus for the separation of particles contained in exhaust gases of internal combustion engines |
| US8444734B2 (en) | 2006-02-20 | 2013-05-21 | Alantum Corporation | Apparatus for the separation of particles contained in exhaust gases of internal combustion engines |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| OP8 | Request for examination as to paragraph 44 patent law | ||
| 8130 | Withdrawal | ||
| 8165 | Unexamined publication of following application revoked |