DE8612624U1 - Device for dedusting and / or detoxifying exhaust gases from thermal processes - Google Patents
Device for dedusting and / or detoxifying exhaust gases from thermal processesInfo
- Publication number
- DE8612624U1 DE8612624U1 DE8612624U DE8612624U DE8612624U1 DE 8612624 U1 DE8612624 U1 DE 8612624U1 DE 8612624 U DE8612624 U DE 8612624U DE 8612624 U DE8612624 U DE 8612624U DE 8612624 U1 DE8612624 U1 DE 8612624U1
- Authority
- DE
- Germany
- Prior art keywords
- dedusting
- exhaust gases
- chambers
- thermal processes
- section
- 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.)
- Expired
Links
Classifications
-
- 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
- B01D46/0039—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with flow guiding by feed or discharge devices
- B01D46/0041—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with flow guiding by feed or discharge devices for feeding
- B01D46/0046—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with flow guiding by feed or discharge devices for feeding provoking a tangential stream
-
- 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
- B01D46/0084—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours provided with safety means
- B01D46/0091—Including arrangements for environmental or personal protection
-
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
- B01D50/20—Combinations of devices covered by groups B01D45/00 and B01D46/00
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C5/00—Apparatus in which the axial direction of the vortex is reversed
- B04C5/08—Vortex chamber constructions
- B04C5/10—Vortex chamber constructions with perforated walls
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C5/00—Apparatus in which the axial direction of the vortex is reversed
- B04C5/12—Construction of the overflow ducting, e.g. diffusing or spiral exits
- B04C5/13—Construction of the overflow ducting, e.g. diffusing or spiral exits formed as a vortex finder and extending into the vortex chamber; Discharge from vortex finder otherwise than at the top of the cyclone; Devices for controlling the overflow
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C5/00—Apparatus in which the axial direction of the vortex is reversed
- B04C5/22—Apparatus in which the axial direction of the vortex is reversed with cleaning means
-
- 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
- C04B38/0003—Porous mortars, concrete, artificial stone or ceramic ware; Preparation thereof containing continuous channels, e.g. of the "dead-end" type or obtained by pushing bars in the green ceramic product
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
- F23J15/022—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material for removing solid particulate material from the gasflow
- F23J15/027—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material for removing solid particulate material from the gasflow using cyclone separators
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2273/00—Operation of filters specially adapted for separating dispersed particles from gases or vapours
- B01D2273/20—High temperature filtration
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Ceramic Engineering (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Toxicology (AREA)
- Structural Engineering (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Cyclones (AREA)
Description
•· ·> · I I ( I I · > a«• · ·> · I I (I I ·> a «
···· ill · · ■···· ill · · ■
** * · · · IfM i * m t 4 * · · · IfM i * mt 4
** ♦·>{·· ι l)i · · · ·· ·· iiili ·· · ι♦ ·> {·· ι l) i · · · ·· ·· iiili ·· · ι
Einrichtung zur Entstaubung Und/oder Entgiftung von
Abgasen aus thermischen ProzessenDevice for dedusting and / or detoxifying
Exhaust gases from thermal processes
Beschreibung:Description:
Die Erfindung betrifft eine Einrichtung zur Entstaubung und/oder Entgiftung von Abgasen aus thermischenThe invention relates to a device for dedusting and / or detoxification of exhaust gases from thermal
Prozessen z.B. Feuerungen, Brennofen in Ziegeleien, ;Processes e.g. furnaces, kilns in brickworks,;
Äbsaughauben, Überschmelzöfen bzw. Gußformen in Gies- ■Suction hoods, melting ovens or casting molds in casting ■
sereien oder Trocknungsanlagen, wobei Staub und/oder |factories or drying systems, whereby dust and / or |
gasförmige Schadstoffe aus den Abgasen entfernt wer- |gaseous pollutants are removed from the exhaust gases
den sollen. \ the should. \
Bekannt sind unter derartigen Einrichtungen speziell ;<
zur Entstaubung solche, bei denen das Gas in ein zyklonartiges Gehäuse wie in einen Zyklonabscheider j
tangential eingeblasen wird. Dabei werden gröbere Teil- | chen an der Gehäuseinnenwand ausgeschleudert und feine |
Teilchen an einem Gewebefilter z.B. aus einem oder meh- p'
reren Schlauchfiltern im Innenraum des zyklonartigen | Gehäuses abgeschieden. Filter aus Geweben oder Faser- |
Vliesen haben aber den Nachteil, daß sie bei heißen Ab- 1 gasen, in denen auch Funken enthalten sein können, sehr
schnell zerstört werden können. '] Among such devices, special devices are known for dust removal in which the gas is blown tangentially into a cyclone-like housing such as a cyclone separator. Coarser partial | thrown on the inside wall of the housing and fine | Particles on a fabric filter, for example from one or more bag filters in the interior of the cyclone-like | Housing deposited. Filters made of fabrics or fiber | However, nonwovens have the disadvantage that they are very hot in the case of hot exhaust gases, which can also contain sparks
can be destroyed quickly. ']
Eine katalytische Umwandlung gasförmiger Schadstoffe \ A catalytic conversion of gaseous pollutants \
ist mit Gewebe- oder Vliesstoff-Filtern im allgemeinen nicht möglich. !is generally not possible with fabric or non-woven fabric filters. !
Aufgabe der Erfindung ist der Einsatz von Filterelementen in einem zyklonartigen Gehäuse, denen hohe Temperaturen
oder Funkenflug nichts anhaben können und die auch
mit katalytisch wirksamen Metallen beschichtet werden
können.The object of the invention is the use of filter elements in a cyclone-like housing, which are not affected by high temperatures or flying sparks, and that too
be coated with catalytically active metals
can.
• · · t «41 «·«• · · t «41« · «
Die Erfindung löst- die Aufgabe gemäß den Schutzansprücheri 1 .- bis 4iThe invention solves the problem according to the protection claims 1 .- to 4i
Die Figuren erläutern die Erfindung an zwei schematisch dargestellten Beispielen: The figures explain the invention using two schematically illustrated examples:
Figur 1 zeigt ein Beispiel nach Schutzansprüöh 1. Figur 2 zeigt ein Beispiel nach Schützänspruch 2.FIG. 1 shows an example according to protection claims 1. Figure 2 shows an example according to Schützänspruch 2.
In Figur 1 wird in das zyklonartige Gehäuse 1 das Abgas 2 tangential eingeblasen. Im Abgas 2 enthaltene Partikel werden durch die Zellenradschleuse 3 oder eine äquivalente Schleuse ausgetragen.In FIG. 1, the exhaust gas 2 is blown tangentially into the cyclone-like housing 1. Particles contained in the exhaust gas 2 are discharged through the rotary valve 3 or an equivalent lock.
Im Gehäuse 1 ist konzentrisch der Rohrkörper 4 aus Keramik - Schaum angeordnet* Dieser ist innenseitig durch radiale Wände 5 in Kammern 6 unterteilt. Bei einem zylindirschen Rohrkörper 4 - wie dargestellt - haben die Kammern 6 den Querschnitt von Kreissegmenten, bei einem polygonförmigen Rohrkörper ist der Querschnitt dreieckförmig. Der Rohrkörper 4 ist unten durch eine Platte 7 oder durch eine entsprechende Scheiben aus Keramik - Schaum abgeschlossen. Oben mündet der Rohrkörper 4 in einen Klappen-Regelapparat 8, in dem nicht dargestellte Verschlußklappen bzw. Ventile für die einzelnen Kammern 6 mit einer Regelautomatik eingebaut sind. Jeweils mindestens eine Kammer wird durch eine Klappe oder ein Ventil verschlossen und gleichzeitig durch einen Druckgas - Strom von innen nach außen beaufschlagt. Das Druckgas wird durch den Kanal 9 in den Regelapparat 8 geleitet. Das der vom Druckgas beaufschlagten Kammer 6 zugeordnete ümfangs - Teilstück des Rohrkörpers 4 wird dabei von außen angelagertem Staub gereinigt. Alle übrigen Kammern 6 sind durch den Regelapparat 8 unmittelbar mit dem Reingasstutzen 10 verbunden, durch den das gereinigte Abgas - beispielsweise über einen Saugzugventilator in einen Kamin - weitergeleitet wird.The tubular body 4 made of ceramic foam is arranged concentrically in the housing 1 * This is through on the inside radial walls 5 divided into chambers 6. In the case of a cylindrical tubular body 4 - as shown - the chambers have 6 shows the cross section of circular segments, in the case of a polygonal tubular body the cross section is triangular. The tubular body 4 is closed at the bottom by a plate 7 or by a corresponding disk made of ceramic foam. At the top, the tubular body 4 opens into a flap control apparatus 8 in which the shutter flaps are not shown or valves for the individual chambers 6 are installed with an automatic control system. At least one chamber each is closed by a flap or valve and at the same time by a pressurized gas flow from the inside to the inside applied externally. The compressed gas is passed through the channel 9 into the control apparatus 8. That of the pressurized gas Chamber 6 assigned circumference - part of the tubular body 4 is cleaned from externally deposited dust. All other chambers 6 are directly connected to the clean gas nozzle 10 by the control apparatus 8, through which the cleaned exhaust gas is passed on - for example via an induced draft fan into a chimney.
In Figur 2 ist praktisch alles analog, nur das ansteile des Rohrkörpers 4 ein - in diesem Beispiel polygonförmiger - äußerer Rohrkörper 11 und ein ebensolcher innerer Rohrkörper 12 angeordnet sind, wobei die radialen Wände 5 nur in dem Ringraum zwischen den beiden Rohrkörpern 11 und 12 die in diesem Falle einen trapezförmigen Quer-Bchnitt aufweisenden Kammern 6 bilden. Durch diese Anordnung zweier oder mehrerer konzentrisch ineinander angeordneter Rohrkörper ist die wirksame Filterfläche wesentlich vergrößert. Alle Funktionen sind analog der Schemadarstei= lung und Beschreibung von Figur 1.In Figure 2, practically everything is analog, only the parts of the tubular body 4 an - in this example polygonal - outer tubular body 11 and an equally such inner one Tubular bodies 12 are arranged, the radial walls 5 only in the annular space between the two tubular bodies 11 and 12 which in this case have a trapezoidal cross-section having chambers 6 form. This arrangement of two or more concentrically arranged one inside the other Tube body, the effective filter area is significantly increased. All functions are analogous to the schema section = development and description of Figure 1.
Die Erfindung beschränkt sich nicht auf diese beiden dargestellten Beispiele. Es könnten auch mehrere Rohrkörper gebündelt wie bei den bekannten Schlauchfilteranlagen im Zentrum eines zyklonartigen Gehäuses angeordnet und über einen entsprechenden Regelapparat zur Druckstoß - Abreinigung jeweils eines einzelnen Rohrkörpers mit dem Reingasstutzen verbunden sein. Ebenso gut könnten auch nach artbekannter Taschenfilter mehrere Filterelemente mit plattenförmigen! Filtermaterial aus Keramik - Schaum gebündelt angeordnet werden.The invention is not limited to these two shown Examples. Several tubular bodies could also be bundled as in the known bag filter systems in the center arranged in a cyclone-like housing and via a corresponding control device for pressure surge cleaning in each case a single pipe body to be connected to the clean gas nozzle. Could just as well be after a well-known species Pocket filter several filter elements with plate-shaped! Ceramic filter material - foam arranged in bundles will.
Die Vorteile der Erfindung gegenüber den bekannten Filtern mit Gewebe- oder Faservliesen sind die bis in sehr hohe Bereiche, beispielsweise bis 1.500 ο c, reichende Temperaturbeständigkeit des Filtermaterials aus Keramik - Schaum, die völlige Unempfindlichkeit dieses Filtermaterials gegen Funkenflug und die zusätzliche Möglichkeit, dieses Filtermaterial mit katalytisch wirksamen Metallen zu beschichten, um zusätzlich zu einer Staubabscheidung eine katalytische Umwandung von Schadgasen im Abgas vornehmen zu können. Dies ist insbesondere dann zweckmäßig, wenn beispielsweise hinter einem Brennofen für Ziegeleierzeugnisse mit organischen Porenbildnern unverbrannte Kohlenwasserstoff - Verbindungen im Abgas des Brennofens enthalten sind.The advantages of the invention over the known filters with fabric or fiber fleeces are that up to very high ranges, for example up to 1,500 ο c, sufficient temperature resistance the filter material made of ceramic foam, the complete insensitivity of this filter material to Flying sparks and the additional possibility of this filter material to be coated with catalytically active metals, in addition to a dust separation, a catalytic To be able to convert harmful gases in the exhaust gas. This is particularly useful when, for example, behind a kiln for brickworks with organic pore formers, unburned hydrocarbon compounds are contained in the exhaust gas of the kiln.
Auch bei zahlreichen arideren thermischen Prozessen befinden sich neben Staub auch gasförmige Schadstoffe iin Abgas, die katalytisch umgewandelt oder unschädlich gemacht wer-Also found in numerous other thermal processes In addition to dust, there are also gaseous pollutants in the exhaust gas, which are catalytically converted or rendered harmless
S den können.S the can.
Claims (4)
Zyklonabscheiders, dadurch gekennzeichnet, daßJ
Cyclone separator, characterized in that
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE8612624U DE8612624U1 (en) | 1986-05-09 | 1986-05-09 | Device for dedusting and / or detoxifying exhaust gases from thermal processes |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE8612624U DE8612624U1 (en) | 1986-05-09 | 1986-05-09 | Device for dedusting and / or detoxifying exhaust gases from thermal processes |
Publications (1)
Publication Number | Publication Date |
---|---|
DE8612624U1 true DE8612624U1 (en) | 1986-08-07 |
Family
ID=6794463
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DE8612624U Expired DE8612624U1 (en) | 1986-05-09 | 1986-05-09 | Device for dedusting and / or detoxifying exhaust gases from thermal processes |
Country Status (1)
Country | Link |
---|---|
DE (1) | DE8612624U1 (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0447802A2 (en) * | 1990-03-21 | 1991-09-25 | Didier-Werke Ag | Vortex finder and method of manufacturing same |
WO1997037746A1 (en) * | 1996-04-08 | 1997-10-16 | K-Tron Technologies, Inc. | Separator for removing fine particulates from air |
EP0972573A1 (en) * | 1998-07-15 | 2000-01-19 | Human net Kabushiki-Kaisya | Cyclone separator and strainer for the same |
WO2012136801A1 (en) * | 2011-04-08 | 2012-10-11 | Beko Technologies Gmbh | Flow-optimized filter head |
ITVR20120089A1 (en) * | 2012-05-11 | 2013-11-12 | Gruppo Piazzetta Spa | HEATING EQUIPMENT |
-
1986
- 1986-05-09 DE DE8612624U patent/DE8612624U1/en not_active Expired
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0447802A2 (en) * | 1990-03-21 | 1991-09-25 | Didier-Werke Ag | Vortex finder and method of manufacturing same |
EP0447802A3 (en) * | 1990-03-21 | 1991-12-18 | Didier-Werke Ag | Vortex finder and method of manufacturing same |
WO1997037746A1 (en) * | 1996-04-08 | 1997-10-16 | K-Tron Technologies, Inc. | Separator for removing fine particulates from air |
US5845782A (en) * | 1996-04-08 | 1998-12-08 | Hurricane Pneumatic Conveying, Inc. | Separator for removing fine particulates from an air stream |
EP0972573A1 (en) * | 1998-07-15 | 2000-01-19 | Human net Kabushiki-Kaisya | Cyclone separator and strainer for the same |
WO2012136801A1 (en) * | 2011-04-08 | 2012-10-11 | Beko Technologies Gmbh | Flow-optimized filter head |
ITVR20120089A1 (en) * | 2012-05-11 | 2013-11-12 | Gruppo Piazzetta Spa | HEATING EQUIPMENT |
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