EP0782477B1 - Cyclone separator - Google Patents
Cyclone separator Download PDFInfo
- Publication number
- EP0782477B1 EP0782477B1 EP95924790A EP95924790A EP0782477B1 EP 0782477 B1 EP0782477 B1 EP 0782477B1 EP 95924790 A EP95924790 A EP 95924790A EP 95924790 A EP95924790 A EP 95924790A EP 0782477 B1 EP0782477 B1 EP 0782477B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- cyclone separator
- separator according
- separation chamber
- separation
- guide
- 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 - Lifetime
Links
- 238000000926 separation method Methods 0.000 claims description 28
- 239000000463 material Substances 0.000 claims description 25
- 238000007654 immersion Methods 0.000 claims description 11
- 238000004804 winding Methods 0.000 claims 3
- 230000009194 climbing Effects 0.000 claims 1
- 230000000007 visual effect Effects 0.000 description 11
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 230000002093 peripheral effect Effects 0.000 description 2
- 230000008092 positive effect Effects 0.000 description 2
- 230000007704 transition Effects 0.000 description 2
- 238000010276 construction Methods 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B7/00—Selective separation of solid materials carried by, or dispersed in, gas currents
- B07B7/08—Selective separation of solid materials carried by, or dispersed in, gas currents using centrifugal force
- B07B7/083—Selective separation of solid materials carried by, or dispersed in, gas currents using centrifugal force generated by rotating vanes, discs, drums, or brushes
-
- 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
- B04C3/00—Apparatus in which the axial direction of the vortex flow following a screw-thread type line remains unchanged ; Devices in which one of the two discharge ducts returns centrally through the vortex chamber, a reverse-flow vortex being prevented by bulkheads in the central discharge duct
- B04C3/06—Construction of inlets or outlets to the vortex chamber
-
- 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
- B04C5/02—Construction of inlets by which the vortex flow is generated, e.g. tangential admission, the fluid flow being forced to follow a downward path by spirally wound bulkheads, or with slightly downwardly-directed tangential admission
- B04C5/04—Tangential inlets
-
- 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
- B04C5/103—Bodies or members, e.g. bulkheads, guides, in the vortex chamber
-
- 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
- B04C9/00—Combinations with other devices, e.g. fans, expansion chambers, diffusors, water locks
Definitions
- the invention relates to a cyclone sifter according to the preamble of claim 1.
- DE-B 10 90 940 is a centrifugal dust separator known, the features of the preamble of claim 1 and in particular has feed channels which are tangential to the Separation room are introduced.
- the channels rise at an angle from bottom to top before they open into the separation area. Details, such as the mouth of the feed channels in the Separation space is formed, DE-B 10 90 940 are not too remove.
- a cyclone separator from EP 398 864 A2 known to separate at least one solid or liquid Substance from a liquid or gaseous medium by centrifugal forces.
- the invention has for its object a cyclone sifter specify with the features of the preamble of claim 1, which with a very simple construction is a very good sighting of the visible material can be achieved.
- the Channel has an area formed as a spiral channel is that the viewing space rises diagonally from bottom to top and flows in a spiral loop into the visual space, and that the spiral channel in the looping area towards the viewing area is open.
- the channel becomes a spiral in the visual space directed upwards and causes that by the Gravity-sinking visible material is repeatedly conveyed upwards is and thus remains in the visual space for a long time. Thereby it is possible to separate the visual goods more precisely what has a positive effect, especially in the middle faction area.
- the coarse material is transferred to the Housing wall crowded and sinks there, while the fines flows out with the classifying air in the central area of the classroom.
- the cyclone classifier has a housing 1 on, which delimits a viewing space 2 in which the visible material by centrifugal forces due to the different weight of the individual particles of the material being sighted.
- Spiral channels 3 and 4 are provided which are diametrically opposed to each other opposite each other and running from bottom to top at 3 'or 4' open into the visual space, whereby they the visible air and the Issue a movement component against gravity.
- the visible material can be shared supplied with the visual air through channels 3, 4 will.
- the visible material can also be passed through channels 5, 6, that open in the area of the upper end of the viewing space 2, are supplied and via a spreading plate 7, which has a Shaft 8 is mounted in the housing 1 and driven by this will be brought into the viewing room 2.
- a spreading plate 7 which has a Shaft 8 is mounted in the housing 1 and driven by this will be brought into the viewing room 2.
- the visible material with the Channels 5, 6 and the spreading disc are supplied with visible air 7 of course not available.
- An immersion tube 9 projects into the viewing space 2 from below Mouth 10 is arranged radially centrally in the viewing space 2.
- the Dip tube 9 can, as shown in Fig. 1, one piece be curved below the mouth 10 and laterally from the Housing 1 are brought out. About the dip tube 9 is Clear air and fines are removed.
- the coarse material sinks at the Outer wall of the housing 1 through an approximately annular space 11, which is formed between the dip tube 9 and the housing wall 1 is down and is via a discharge opening 19th dissipated.
- a guide device is located on the dip tube 9 in the region of its mouth 10 12 arranged.
- the guide device 12 is a conical one Sheet metal ring that with its upper edge with smaller Diameter attached to the outside of the dip tube 9 gas-tight is, whereas its lower edge is larger in diameter protrudes all around from the outer peripheral surface of the dip tube 9. This guide device 12 has the following effect:
- the guide device 12 hardly changes the Peripheral speed (flow conditions) and thus the Centrifugal forces in the viewing area 2 in the approximately annular space 11 by the curved lead out Dip tube 9 occurring flow disturbances from the viewing area 2 shielded.
- the guide ring 13 has the shape of a top and bottom tapered jacket of a truncated cone and is gas-tight with its upper edge with a larger diameter attached to the inside of the housing wall 1, whereas be lower edge with a smaller diameter compared to the edge of the Housing 1 is offset inwards.
- the guide ring 13 is thus from the wall of the housing 1 downwards and inwards.
- baffles 20 are attached, which inwards protrude the viewing space 2. These baffles 20 contribute to one Rinsing the visible material flung against the housing wall 1 at, which in particular the finer visible material back in the visual space 2 is carried back because the space between the Baffles 20 from that fed through the channels 3, 4 Visible air is flushed out.
- the baffles 20 extend as shown in Fig. 1 only on a single baffle 20 is, either over the entire height of the viewing space 2 to Guide ring 13 down or just about the height of merging channels 3, 4.
- a number of guide vanes 14 may be provided, which on Dip tube 9 in the area of the transition of the viewing space 2 in an outflow chamber 15 are arranged.
- the outflow space 15 is the space that is approximately in the axial extension of the dip tube 9 extends upwards.
- the guide vanes 14 are, as can be seen in FIG. 7, in the Cross-section curved and can preferably be adjustable, to the respective circumstances, especially the flow rate to be able to adapt. Through the guide vanes 14 ensures that the classifying air with the fine material largely undisturbed from the rotating in the radial direction of movement and can go further into the axial, whereby the flow resistances decrease, which in turn affects the necessary energy use has a positive effect.
- the guide vanes 14 can be arranged so that they extending from the opening 10 of the dip tube 9 upwards incline towards the main axis 16 of the cyclone sifter, whereby the Transition of the flow from the radial to the axial direction is further improved.
- a classifier wheel 17 with blades can also be used 18 can be provided to the coarse material even better from the fines separate.
- the classifier wheel 17 rotates outside the guide vanes 14 and extends substantially over the entire Height of the viewing area 2.
- the invention can be as follows, for example being represented:
- the cyclone classifier has a housing 1, which approximately one encloses rotationally symmetrical viewing space 2, and one Device 3, 4 for supplying visual air and optionally Visible material in the viewing space 2, which is approximately tangential in the viewing space 2 flows.
- the cyclone classifier also has an outlet 19 for coarse material and an immersion tube 9 for removing the visual air with Fine goods on.
- the device for supplying visual air is formed by two channels 3, 4, which spiral around the The main axis 16 of the cyclone sifter is curved into the viewing space 2 flow into.
Description
Die Erfindung betrifft einen Zyklonsichter gemäß dem Oberbegriff
des Patentanspruches 1.The invention relates to a cyclone sifter according to the preamble
of
Aus der DE-B 10 90 940 ist ein Fliehkraft-Staubabscheider
bekannt, der die Merkmale des Oberbegriffes des Anspruches 1
und insbesondere Zuführkanäle aufweist, die tangential an den
Trennraum herangeführt sind. Die Kanäle steigen dabei schräg
von unten nach oben an bevor sie in den Trennraum einmünden.
Details, wie der Einmündungsbereich der Zuführkanäle in den
Trennraum ausgebildet ist, sind der DE-B 10 90 940 nicht zu
entnehmen.From DE-B 10 90 940 is a centrifugal dust separator
known, the features of the preamble of
Des weiteren ist ein Zyklonabscheider aus der EP 398 864 A2 bekannt, der zum Abtrennen wenigstens eines festen oder flüssigen Stoffes aus einem flüssigen oder gasförmigen Medium durch Zentrifugalkräfte dient.Furthermore, a cyclone separator from EP 398 864 A2 known to separate at least one solid or liquid Substance from a liquid or gaseous medium by centrifugal forces.
Der Erfindung liegt die Aufgabe zugrunde, einen Zyklonsichter
mit den Merkmalen des Oberbegriffes des Anspruches 1 anzugeben,
bei dem mit einer sehr einfachen Konstruktion eine sehr
gute Sichtung des Sichtgutes erzielt werden kann.The invention has for its object a cyclone sifter
specify with the features of the preamble of
Gelöst wird diese Aufgabe erfindungsgemäß dadurch, daß der Kanal einen Bereich aufweist, der als Spiralkanal ausgebildet ist, der den Sichtraum schräg von unten nach oben ansteigend und spiralförmig umschlingend in den Sichtraum einmündet, und daß der Spiralkanal im Umschlingungsbereich zum Sichtraum hin offen ist.This object is achieved in that the Channel has an area formed as a spiral channel is that the viewing space rises diagonally from bottom to top and flows in a spiral loop into the visual space, and that the spiral channel in the looping area towards the viewing area is open.
Durch den wenigstens einen schräg nach oben in den Sichtraum einmündenden Kanal wird die Luft schraubenförmig im Sichtraum nach oben gerichtet und bewirkt dadurch, daß das durch die Schwerkraft absinkende Sichtgut wiederholt nach oben gefördert wird und somit eine längere Zeit im Sichtraum verweilt. Dadurch ist es möglich, das Sichtgut genauer zu trennen, was sich insbesondere im mittleren Fraktionsbereich positiv auswirkt. Das Grobgut wird dabei durch die Fliehkraft an die Gehäusewand gedrängt und sinkt dort ab, wogegen das Feingut mit der Sichtluft im zentralen Bereich des Sichtraumes abströmt.Through the at least one diagonally upwards into the viewing room The channel becomes a spiral in the visual space directed upwards and causes that by the Gravity-sinking visible material is repeatedly conveyed upwards is and thus remains in the visual space for a long time. Thereby it is possible to separate the visual goods more precisely what has a positive effect, especially in the middle faction area. The coarse material is transferred to the Housing wall crowded and sinks there, while the fines flows out with the classifying air in the central area of the classroom.
Dieser erhebliche Vorteil der längeren Verweildauer des Sichtgutes im Sichtraum wird dabei auf sehr einfach Weise erzielt, ohne daß es zu einem erhöhten technischen Aufwand des Zyklonsichters kommt.This considerable advantage of the longer dwell time of the material to be viewed in the visual space it is achieved in a very simple way, without causing an increased technical effort for the cyclone sifter is coming.
Bevorzugte und vorteilhafte Ausgestaltungen des erfindungsgemäßen
Zyklonsichters sind Gegenstand der Unteransprüche und
werden nachfolgend unter Bezugnahme auf die Zeichnungen näher
erläutert. Es zeigt:
Wie bei der in Fig. 1 und 2 dargestellten Ausführungsform der
Erfindung zu sehen ist, weist der Zyklonsichter ein Gehäuse 1
auf, das einen Sichtraum 2 begrenzt, in welchem das Sichtgut
durch Zentrifugalkräfte auf Grund des unterschiedlichen Gewichtes
der einzelnen Partikel des Sichtgutes gesichtet wird.As in the embodiment of FIGS. 1 and 2
Invention can be seen, the cyclone classifier has a
Zum Zuführen von Sichtluft und gegebenfalls Sichtgut sind zwei
spiralförmige Kanäle 3 und 4 vorgesehen, die einander diamentral
gegenüberliegen und von unten nach oben verlaufend bei 3' bzw. 4'
in den Sichtraum einmünden, wodurch sie der Sichtluft und dem
Sichtgut eine Bewegungskomponente gegen die Schwerkraft erteilen.There are two for supplying classifying air and possibly classifying
Das Sichtgut kann in einer Ausführungsform der Erfindung gemeinsam
mit der Sichtluft durch die Kanäle 3, 4 zugeführt
werden. In einer anderen, in Fig. 1 dargestellten Ausführungsform
der Erfindung kann das Sichtgut auch durch Kanäle 5, 6,
die im Bereich des oberen Endes des Sichtraumes 2 münden,
zugeführt werden und über einen Streuteller 7, der über eine
Welle 8 im Gehäuse 1 gelagert ist und über diese angetrieben
wird, in den Sichtraum 2 eingebracht werden. Wird bei der in
Fig. 1 dargestellten Ausführungsform das Sichtgut mit der
Sichtluft zugeführt, sind die Kanäle 5, 6 und der Streuteller
7 natürlich nicht vorhanden.In one embodiment of the invention, the visible material can be shared
supplied with the visual air through
In den Sichtraum 2 ragt von unten ein Tauchrohr 9, dessen
Mündung 10 radial mittig im Sichtraum 2 angeordnet ist. Das
Tauchrohr 9 kann, wie in Fig. 1 dargestellt ist, ein Stück
unterhalb der Mündung 10 gekrümmt sein und seitlich aus dem
Gehäuse 1 herausgeführt werden. Über das Tauchrohr 9 wird
Sichtluft und Feingut abgeführt. Das Grobgut sinkt an der
Außenwand des Gehäuses 1 durch einen etwa ringförmigen Raum
11, der zwischen dem Tauchrohr 9 und der Gehäusewand 1 gebildet
wird, nach unten ab und wird über eine Austragöffnung 19
abgeführt.An
Am Tauchrohr 9 ist im Bereich seiner Mündung 10 eine Leiteinrichtung
12 angeordnet. Die Leiteinrichtung 12 ist ein konischer
Blechring, der mit seinem oberen Rand mit kleinerem
Durchmesser an der Außenseite des Tauchrohres 9 gasdicht befestigt
ist, wogegen sein unterer Rand mit größerem Durchmesser
ringsum von der Außenumfangsfläche des Tauchrohres 9 absteht.
Diese Leiteinrichtung 12 hat folgende Wirkung:A guide device is located on the
Die Leiteinrichtung 12 führt kaum zu einer Veränderung der
Umfangsgeschwindigkeit (Strömungsverhältnisse) und damit der
Fliehkräfte im Sichtraum 2. Durch die Leiteinrichtung 12 werden
im etwa ringförmigen Raum 11 durch das gekrümmt herausgeführte
Tauchrohr 9 auftretende Strömungsstörungen vom Sichtraum
2 abgeschirmt.The
Die vorteilhafte Wirkung der Leiteinrichtung 12, die wie in
Fig. 5 dargestellt, auch doppelt vorgesehen sein kann, kann
durch einen Leitring 13, der bei allen Ausführungsformen des
erfindungsgemäßen Zyklonsichters vorgesehen sein kann, noch
verbessert werden. Der Leitring 13 hat die Form eines sich von
oben nach unten verjüngenden Mantels eines Kegelstumpfes und
ist mit seinem oberen Rand mit größerem Durchmesser gasdicht
an der Innenseite der Gehäusewand 1 befestigt, wogegen sein
unterer Rand mit kleinerem Durchmesser gegenüber dem Rand des
Gehäuses 1 nach innen versetzt ist. Der Leitring 13 steht also
von der Wand des Gehäuses 1 nach unten und innen ab.The advantageous effect of the
An der innenwand des Gehäuses 1 können, wie in Fig. 2 dargestellt
ist, Leitbleche 20 befestigt sein, die nach innen in
den Sichtraum 2 abstehen. Diese Leitbleche 20 tragen zu einer
Durchspülung des an die Gehäusewand 1 geschleuderten Sichtgutes
bei, wodurch insbesondere das feinere Sichtgut wieder in
den Sichtraum 2 zurückgetragen wird, da der Raum zwischen den
Leitblechen 20 von der durch die Kanäle 3, 4 zugeführten
Sichtluft durchspült wird. Die Leitbleche 20 erstrecken sich,
wie in Fig. 1 nur an einem einzigen Leitblech 20 dargestellt
ist, entweder über die gesamte Höhe des Sichtraumes 2 bis zum
Leitring 13 nach unten oder auch nur etwa über die Höhe der
einmündenden Kanäle 3, 4.On the inner wall of the
Um das Strömungsverhalten im Zyklonsichter zu verbessern, d.h.
die Strömung besser zu richten und Wirbel abzubauen, kann in
einer in Fig. 7 dargestellten Ausführungsform der Erfindung
auch eine Anzahl von Leitschaufeln 14 vorgesehen sein, die am
Tauchrohr 9 im Bereich des Überganges des Sichtraumes 2 in
einen Abströmraum 15 angeordnet sind. Der Abströmraum 15 ist
jener Raum, der sich etwa in axialer Verlängerung des Tauchrohres
9 nach oben erstreckt.To improve the flow behavior in the cyclone classifier, i.e.
To straighten the flow better and reduce eddies can
an embodiment of the invention shown in Fig. 7
also a number of
Die Leitschaufeln 14 sind, wie in Fig. 7 zu sehen ist, im
Querschnitt gekrümmt und können vorzugsweise verstellbar sein,
um sie den jeweiligen Gegebenheiten, insbesondere der Strömungsgeschwindigkeit
anpassen zu können. Durch die Leitschaufeln
14 wird sichergestellt, daß die Sichtluft mit dem Feingut
weitgehend ungestört von der drehenden in die radiale Bewegungsrichtung
und weiter in die axiale übergehen kann, wodurch
die Strömungswiderstände sinken, was sich wiederum auf den
erforderlichen Energieeinsatz positiv auswirkt. Vorzugsweise
können die Leitschaufeln 14 dabei so angeordnet sein, daß sie
sich von der Öffnung 10 des Tauchrohres 9 ausgehend nach oben
zur Hauptachse 16 des Zyklonsichters hin neigen, wodurch der
Übergang der Strömung von der radialen in die axiale Richtung
weiter verbessert wird.The
Zusätzlich kann weiters noch ein Sichterrad 17 mit Schaufeln
18 vorgesehen sein, um das Grobgut noch besser vom Feingut zu
trennen. Das Sichterrad 17 dreht sich außerhalb der Leitschaufeln
14 und erstreckt sich im wesentlichen über die gesamte
Höhe des Sichtraumes 2.In addition, a
Es versteht sich, daß, um eine höhere Durchsatzleistung des
erfindungsgemäßen Zyklonsichters erzielen zu können, mehr als
zwei Zuführkanäle vorgesehen sein können. Weiters kann zusätzlich
zu dem in den Figuren dargestellten unteren Tauchrohr 9
ein zweites Tauchrohr vorgesehen sein, das dem unteren Tauchrohr
9 gegenüberliegend von oben in das Gehäuse 1 und den
Sichtraum 2 ragt.It is understood that in order to achieve a higher throughput of the
To achieve cyclone classifier according to the invention, more than
two feed channels can be provided. Furthermore, additional
to the
Zusammenfassend kann die Erfindung beispielsweise wie folgt dargestellt werden:In summary, the invention can be as follows, for example being represented:
Der Zyklonsichter weist ein Gehäuse 1 auf, das einen etwa
rotationssymmetrischen Sichtraum 2 umschließt, sowie eine
Einrichtung 3, 4 zum Zuführen von Sichtluft und gegebenenfalls
Sichtgut in den Sichtraum 2, die etwa tangential in den Sichtraum
2 mündet. Der Zyklonsichter weist weiters einen Auslaß 19
für Grobgut und ein Tauchrohr 9 zum Abführen der Sichtluft mit
Feingut auf. Die Einrichtung zum Zuführen von Sichtluft wird
durch zwei Kanäle 3, 4 gebildet, die spiralförmig um die
Hauptachse 16 der Zyklonsichters gekrümmt in den Sichtraum 2
einmünden.The cyclone classifier has a
Claims (20)
- Cyclone separator with a vertical principal axis (16), having a housing (1) surrounding an approximately rotationally symmetrical separation chamber (2), having at least one duct (3, 4) for supplying separation air and, optionally, material for separation into the separation chamber, the duct leading approximately tangentially to the separation chamber (2), having a discharge opening (19) for coarse material and having an outlet (10) for the separation air with fine material, characterised in that the duct (3, 4) has a region which is in the form of a spiral duct (3', 4') which, climbing the separation chamber (2) diagonally from the bottom to the top and winding round it in the form of a spiral, opens out into the separation chamber (2), in that the spiral duct (3', 4') is open, in the winding region, towards the separation chamber (2), and in that the opening at the beginning of the winding region is at a distance from the upper end of the separation chamber (2).
- Cyclone separator according to claim 1, characterised in that at least two ducts (3, 4) arranged diametrically opposite one another are provided for supplying separation air.
- Cyclone separator according to claim 2, characterised in that the outlet (10) for the separation air and fine material is a mouth of an immersion pipe (9) opening into the separation chamber centrally and from below.
- Cyclone separator according to claim 3, further characterised in that an immersion pipe protruding into the separation chamber (2) centrally and from above is provided for removing the separation air and fine material.
- Cyclone separator according to any one of claims 1 to 4, characterised in that a device (7, 8), preferably in the form of a distributing plate, for supplying material for separation is arranged in the upper region of the separation chamber (2).
- Cyclone separator according to any one of claims 3 to 5, characterised in that a guide device (12) is arranged on the lower immersion pipe (9) near to the mouth (10).
- Cyclone separator according to claim 6, characterised in that the guide device (12) tapers conically in an upward direction towards the mouth (10) of the immersion pipe (9).
- Cyclone separator according to claim 6 or claim 7, characterised in that more than one guide device (12), preferably two guide devices (12), in the form of truncated cone casings which taper towards the mouth (10) of the immersion pipe (9), are provided on the lower immersion pipe (9).
- Cyclone separator according to any one of claims 3 to 8, characterised in that an inwardly protruding guide ring (13) is arranged on the wall of the housing (1) in the region of the separation chamber (2) and in the region of the mouth (10) of the lower immersion pipe (9).
- Cyclone separator according to claim 9, characterised in that the guide ring (13) is in the form of a truncated cone casing which tapers from the top to the bottom.
- Cyclone separator according to any one of claims 1 to 10, characterised in that the discharge opening (19) for coarse material is arranged at the lower end of a substantially ring-shaped chamber (11) delimited by the housing (1) and by the lower immersion pipe (9).
- Cyclone separator according to any one of claims 1 to 11, characterised in that guide vanes (14) are arranged in the separation chamber (2).
- Cyclone separator according to claim 12, characterised in that the guide vanes (14) extend approximately over the axial extension of the separation chamber (2).
- Cyclone separator according to claim 12 or claim 13, characterised in that the separation chamber (2) surrounds an air exhaust chamber (15) arranged centrally and in the axial (16) extension of the device (10) for removing separation air and fine material, and in that the guide vanes (14) are arranged in the border region between the separation chamber (2) and the air exhaust chamber (15).
- Cyclone separator according to claim 14, characterised in that the guide vanes (14) protrude into the air exhaust chamber (15).
- Cyclone separator according to any one of claims 1 to 15, characterised in that the guide vanes (14) have a curved cross-section.
- Cyclone separator according to any one of claims 1 to 16, characterised in that the guide vanes (14) are adjustable in terms of their radial orientation.
- Cyclone separator according to any one of claims 1 to 17, characterised in that guide plates (20) projecting inwards into the separation chamber (2) are arranged on the inner wall of the housing (1).
- Cyclone separator according to claim 18, characterised in that the guide plates (20) extend over the entire height of the separation chamber (2).
- Cyclone separator according to claim 18, characterised in that the guide plates (20) extend approximately over the height of the spiral ducts (3', 4').
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE4434038A DE4434038A1 (en) | 1994-09-23 | 1994-09-23 | Device for separating at least one substance from a medium |
DE4434038 | 1994-09-23 | ||
PCT/AT1995/000154 WO1996009120A1 (en) | 1994-09-23 | 1995-07-26 | Cyclone separator |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0782477A1 EP0782477A1 (en) | 1997-07-09 |
EP0782477B1 true EP0782477B1 (en) | 1998-09-16 |
Family
ID=6529023
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP95924790A Expired - Lifetime EP0782477B1 (en) | 1994-09-23 | 1995-07-26 | Cyclone separator |
Country Status (6)
Country | Link |
---|---|
EP (1) | EP0782477B1 (en) |
CZ (1) | CZ292180B6 (en) |
DE (2) | DE4434038A1 (en) |
HU (1) | HUT77213A (en) |
PL (1) | PL319302A1 (en) |
WO (1) | WO1996009120A1 (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AT413339B (en) * | 2003-12-30 | 2006-02-15 | Pmt Gesteinsvermahlungstechnik | LEADING DEVICE FOR FLOWERS, ESPECIALLY CYCLONE SEPARATORS |
WO2012019624A1 (en) * | 2010-08-11 | 2012-02-16 | Fmc Technologies C.V. | High efficiency phase splitter |
CN102527176A (en) * | 2011-12-15 | 2012-07-04 | 常熟市上海飞奥压力容器制造有限公司 | Vertical natural gas filter |
AT512151B1 (en) * | 2012-05-24 | 2013-06-15 | A Tec Holding Gmbh | Device for separating substances from a medium |
DE102019123034B3 (en) * | 2019-08-28 | 2020-12-03 | Khd Humboldt Wedag Gmbh | Cyclone with rotating rod basket |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1960887A (en) * | 1931-09-24 | 1934-05-29 | Alexander William | Dust separator |
GB517206A (en) * | 1938-08-26 | 1940-01-23 | Andrew Thomson Bowden | Process and apparatus for separating solid particles from gases |
DE1090940B (en) * | 1954-07-30 | 1960-10-13 | Reinhold Kamps Dipl Ing Dr | Centrifugal dust separator with one or more cyclones arranged in a housing, especially for cracking plants |
DE2137128C3 (en) * | 1971-07-24 | 1978-10-05 | Siemens Ag, 1000 Berlin Und 8000 Muenchen | Device for generating swirl in a rotary flow vortex |
DE3808023A1 (en) * | 1988-03-10 | 1989-09-21 | Krupp Polysius Ag | Separator |
FI902329A0 (en) * | 1989-05-18 | 1990-05-09 | Voest Alpine Krems | AVSKILJNINGSFOERFARANDE OCH -ANORDNING. |
JP2509374B2 (en) * | 1990-07-23 | 1996-06-19 | 株式会社クボタ | Granule classifier |
JPH05232177A (en) * | 1992-02-24 | 1993-09-07 | Nec Corp | Method for inspecting printed wiring board |
-
1994
- 1994-09-23 DE DE4434038A patent/DE4434038A1/en not_active Withdrawn
-
1995
- 1995-07-26 WO PCT/AT1995/000154 patent/WO1996009120A1/en active IP Right Grant
- 1995-07-26 EP EP95924790A patent/EP0782477B1/en not_active Expired - Lifetime
- 1995-07-26 DE DE59503633T patent/DE59503633D1/en not_active Expired - Fee Related
- 1995-07-26 PL PL95319302A patent/PL319302A1/en unknown
- 1995-07-26 HU HU9701735A patent/HUT77213A/en unknown
- 1995-07-26 CZ CZ1997878A patent/CZ292180B6/en not_active IP Right Cessation
Also Published As
Publication number | Publication date |
---|---|
WO1996009120A1 (en) | 1996-03-28 |
DE59503633D1 (en) | 1998-10-22 |
CZ87897A3 (en) | 1997-07-16 |
EP0782477A1 (en) | 1997-07-09 |
PL319302A1 (en) | 1997-08-04 |
HUT77213A (en) | 1998-03-02 |
DE4434038A1 (en) | 1996-03-28 |
CZ292180B6 (en) | 2003-08-13 |
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