EP0155556B1 - Air suction device for a sifting or sorting apparatus - Google Patents

Air suction device for a sifting or sorting apparatus Download PDF

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Publication number
EP0155556B1
EP0155556B1 EP85102170A EP85102170A EP0155556B1 EP 0155556 B1 EP0155556 B1 EP 0155556B1 EP 85102170 A EP85102170 A EP 85102170A EP 85102170 A EP85102170 A EP 85102170A EP 0155556 B1 EP0155556 B1 EP 0155556B1
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EP
European Patent Office
Prior art keywords
air
suction channel
air distribution
distribution chamber
stand
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EP85102170A
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German (de)
French (fr)
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EP0155556A2 (en
EP0155556A3 (en
Inventor
Roman Mueller
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Buehler AG
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Buehler AG
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Priority to AT85102170T priority Critical patent/ATE56158T1/en
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B07SEPARATING SOLIDS FROM SOLIDS; SORTING
    • B07BSEPARATING 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
    • B07B9/00Combinations of apparatus for screening or sifting or for separating solids from solids using gas currents; General arrangement of plant, e.g. flow sheets
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B07SEPARATING SOLIDS FROM SOLIDS; SORTING
    • B07BSEPARATING 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
    • B07B1/00Sieving, screening, sifting, or sorting solid materials using networks, gratings, grids, or the like
    • B07B1/46Constructional details of screens in general; Cleaning or heating of screens
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B07SEPARATING SOLIDS FROM SOLIDS; SORTING
    • B07BSEPARATING 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
    • B07B4/00Separating solids from solids by subjecting their mixture to gas currents
    • B07B4/08Separating solids from solids by subjecting their mixture to gas currents while the mixtures are supported by sieves, screens, or like mechanical elements
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B07SEPARATING SOLIDS FROM SOLIDS; SORTING
    • B07BSEPARATING 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
    • B07B2201/00Details applicable to machines for screening using sieves or gratings
    • B07B2201/04Multiple deck screening devices comprising one or more superimposed screens

Definitions

  • the invention relates to a device for extracting air for sighting or classifying devices according to the preamble of claim 1.
  • Sighting and classifying devices are special machines that are used in large numbers in grain milling. It is used to separate grain as well as regrind into the desired fraction.
  • a work table forms the heart of the device, through which the material to be separated is conveyed by a vibration movement. Supported by an air velocity that is adapted to the fineness of the product, the goods are separated according to their weight as well as their size or a corresponding form factor.
  • a prerequisite for high separation quality is, in particular, a quantity of air that can be controlled over the entire length of the machine, for which purpose an upwardly tapering air distribution space with a number of approximately 10 to 20 air duct chambers is used.
  • a throttle element is assigned to each air guide chamber or bulkhead, with which the amount of air can be adjusted in accordance with the desired separation work.
  • This centrifugal separator has in its center a suction channel running transversely to the flow direction within the separator. Air and lighter particles carried on the inner wall of the centrifugal separator can be drawn off via individual openings in the outer wall of the transverse suction channel. Heavier particles, which move closer to the inner wall compared to the lighter particles in the centrifugal separator, are excreted at their opening in the outer wall after separation in the centrifugal separator so that they are not yet completely circulated.
  • this device has the disadvantage that the homogeneous air flow is disturbed due to the edges of the openings in the suction channel, but also due to the edges of the opening in the outer wall of the centrifugal separator. At these points, air vortices arise, but also dead spaces in which material is undesirably deposited, which worsens the flow properties within and thus the suction and separation effect of the device as a whole.
  • a similar device is known from DE-A-2 342 091, in which a deflection sifter which is curved approximately 180 ° in a circular manner also has in its center a separating channel which runs transversely to the flow direction in the deflection sifter.
  • coal grains are to be freed of dust-like particles adhering to the surface and the coal fraction lying above 0.5 mm is thrown out of the gas flow during the 180 ° deflection in the classifier and discharged via a line into a setting machine.
  • the dust-like fraction below 0.5 mm is removed with the gas flow through the gas exhaust pipe arranged on the deflector into a dust separator.
  • Vortexes also occur in this gas stream, whereby in addition to the disadvantages already described in AU-B-483 698 with regard to vortex formation such as this, a flap which changes the free flow cross section in the flow beginning region of the deflector sifter very quickly has particle deposits which immediately cause a disturbance the function of this valve.
  • a suction channel is known which is partially installed or embedded in a hood similar to an air distribution space.
  • the sucked-in air sweeps in opposite directions on both inner sides of the suction channel, and the air flow vortices thus formed mutually eliminate each other when they meet.
  • undesired dead spaces ultimately arise, which lead to undesired product deposits and require frequent and time-consuming cleaning.
  • the object of the invention is to eliminate these disadvantages as far as possible with a simple structure.
  • the tan gential transition creates a cyclone flow in the suction channel, which has the advantage that neither dust nor other particles can be deposited.
  • the invention thus not only ensures that the machine is kept clean, but also improves its operational safety.
  • the throttles can be arranged in the transition area between the air distribution space and the suction duct, which results not only in a compact design but also in a favorable guidance of the air flow, because the transition area and the throttles form only one common disturbance in the air flow.
  • the throttles are very particularly preferably designed as adjusting slides. It has been shown that, in connection with the tangential transition from the air distribution space into the suction channel, adjustment slides allow a very precise and almost linear adjustment of the local air flow rate over a wide range, since the deflection angles for the air flow are changed only slightly.
  • the throttle elements can preferably be designed as adjusting flaps and, seen in the direction of flow of the air, can be arranged behind the air distribution space.
  • a further, very advantageous embodiment of the device according to the invention also consists in the suction channel being designed as a separate component and the air distribution space being placed as a lying cyclone (“backpack-like”).
  • backpack-like the air distribution space
  • the suction channel has a constant cross section.
  • the suction channel is at least partially rounded in cross section, preferably circular. It has also proven to be particularly favorable if the diameter of the cross section of the suction channel is approximately one third to one fourth the width of the sieve layers.
  • FIGS. 1 and 2 in which a so-called “double machine” is shown, which consists of two semolina cleaning machines that are completely separate in terms of working technology, as shown in FIG. 2. These two semolina cleaning machines are arranged on the left and right with respect to a central stand construction.
  • each individual collecting device 4 or 5 has two processes 6 or 7.
  • the sieve layers 3 are each combined to form a cleaning box 8 (FIG. 2), so that each cleaning box 8 is assigned two outlets 2 for the screen rejection and four outlets 6 and 7 for the screen diarrhea in accordance with the illustrated embodiment.
  • Each cleaning box 8 is supported by an end support 12 (FIG.
  • the collecting device 4 is designed as a vibrating conveyor trough, which rests on both end sides on a support 19 mounted in rubber (FIG. 1).
  • the oscillation drive of the collecting device 4 takes place via a lever 20 which connects the oscillating end support 12 to the support 19.
  • the swing stroke of the collecting device 4 can thus be selected or adjusted independently of the swing stroke of the cleaning box 8.
  • the stand 9 carries all non-vibrating components directly, the vibrating elements being mounted above the lower part of the stand.
  • the stand 9 also has a vertical support 21 on each end side (FIG. 2), which merges into a foot construction at the bottom via an extension. According to the illustration in FIG.
  • the vertical support 21 extends a little beyond the uppermost sieve position and supports the stand head 11, which essentially forms the upper air distribution space 22.
  • This upper air distribution chamber 22 has a tapered shape and is upwardly g over its length by bulkheads 23 into sixteen separate Beer DINun shuntn 24 divided.
  • the bulkheads 23, as can be seen in FIG. 1, are brought close to the uppermost sieve layer, the distance being chosen so that it is somewhat larger than the greatest layer thickness "S" of the material which ever occurs (see FIG. 3 and Fig. 5).
  • the upper inclined surfaces of the air distribution space 22 have transparent windows 25 over their entire length (FIG. 2), so that the flow behavior of the material over the top sieve layer 3 can be controlled with an electric light source from the outside of the device. 3 and 4 can be seen between the upper end of the air distribution space 22 and one sitting on the air distribution space 22.
  • Suction manifold 27 throttles in the form of adjusting flaps 28, which can be individually adjusted according to the respective air requirement via a head 29. 3 to 6 show, the inner walls of the air distribution space and the suction duct adjoin one another in a transition area such that the air passes tangentially into the suction duct, so that a cyclone flow forms in the suction duct.
  • the vibrator 14 When the semolina cleaning machine shown is started up, the vibrator 14 is switched on so that the cleaning box 8, the bottom 32 and the collecting devices 4 and 5 carry out the preselected oscillating movement in the longitudinal direction of the device. Likewise, the entire device is placed in a slight negative pressure via the suction collecting duct 27 or an aspiration associated therewith. Depending on the separation task, all slides and flaps 28 are provisionally adjusted, after which the product can be fed into the inlet 1. The product immediately falls on the top sieve layer 3. Due to the shaking movement which is imprinted on the material, as well as the sieve layers deliberately inclined downwards from the inlet 1 to the outlet 2 and the air flow through the sieve layers 3, the product behaves like a liquid (fluidized ).
  • the central task of the semolina cleaning machine lies in the actual sieving process. So the air flow must not be adjusted so much that the entire product layer could be lifted off the sieve layers. Rather, the air primarily serves the function of locating the product and distributing it evenly over the entire surface.
  • the product should be fractionated into coarse, medium and fine size or into cooking size and medium size etc.
  • the first six chutes 34 can be directed into the collecting device 4, the subsequent eleven chutes 34 into the collecting device 5.
  • the two sieve passes are finished products that can be delivered to the corresponding storage cells or to the consumers.
  • the screen rejects at the outlets 2 are partially re-ground or comminuted and then reach a second, appropriately set, semolina cleaning machine.
  • the miller's actual task begins, namely the assessment of the functioning of the device and the quantitative and qualitative assessment of the fractions obtained.
  • the light source 26 (FIG. 2) is switched on, so that the entire space within the air distribution space 22 is illuminated.
  • the flow behavior of the product within the individual air guide chambers 24 can be observed through the windows 25 over the entire length. If an image similar to the boiling water appears in one or more air guiding chambers 24, the amount of air in the relevant air guiding chambers 24 is throttled via the adjustment flaps 28. Conversely, a jam can also occur at individual points: here the local air volume must be increased accordingly. If the flow behavior of the product is flawless and if there are no parts in the mixed product (outlets) that belong to sieve diarrhea, the quality of the sieve diarrhea is checked again and the chutes 34 are adjusted to the correct collecting devices 4 and 5, respectively.
  • two different processes 6 and 7 can be selected from each collecting device 4 or 5, so that four different fractions can be separated from each cleaning box 8.
  • the cross section of the suction channel 27 increases in the direction of the air flow.
  • FIGS. 5 and 6 show, as an alternative to FIGS. 3 and 4, a further advantageous embodiment.
  • sliders 40 are used in the solution of FIGS. 5 and 6. These sliders 40 allow more precise adjustment of the air requirement in all slider positions. A proportional change in cross-section of the slide opening is caused in accordance with the revolutions of the head 29. If a flap 28 were used instead of a slider 40, no similar, proportional cross-sectional change would occur in this case, however, since in such a case the effective opening cross-section would no longer change in proportion to the rotation of the head 29.
  • the slide solution also has the further advantage that the free cross section of the suction collecting duct 27 is not influenced by the different open positions of the slide 40.
  • the suction collecting duct 27 can be designed with a constant cross section in the air flow direction.
  • the suction device according to the invention can also be used in particular in separation devices which primarily work according to their weight, as well as in different versions of light-grain readers and also in combined machines. Work processes are always carried out by the machines mentioned, in which larger work surfaces in a plurality smaller, controllable areas of the air volume must be divided, but it must be possible to control the air volume only above the bed layer (usually on the suction side). This gives good controllability of the air volume for suction operation without the disadvantages that often occur in the prior art due to the strong dusting of the corresponding throttle ducts.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Combined Means For Separation Of Solids (AREA)
  • Cleaning In General (AREA)
  • Peptides Or Proteins (AREA)
  • Manipulator (AREA)
  • Sorting Of Articles (AREA)
  • Pretreatment Of Seeds And Plants (AREA)
  • Detergent Compositions (AREA)

Abstract

In the case of an apparatus for cleaning grits, which has a plurality of superimposed screen layers, which can be vibrated by means of at least one unbalance exciter and with an inlet or outlet for the product inlet or screen discharge arranged at one end, collecting means with adjustable setting flaps for the screenings, as well as an air circulation through the screen layers over an air distribution chamber in a suction collecting channel adjustable by means of adjusting flaps, it is provided that the apparatus is constructed as a stand with a stand head, a stand base and a vertical intermediate support connecting said two parts, the screen layers being constructed as a dust box and being vibratably supported in the vicinity of the stand base, the stand top being formed by the upper air distribution chamber.

Description

Die Erfindung betrifft eine Vorichtung zum Absaugen von Luft für Sicht- oder Klassiervorrichtungen nach dem Oberbegriff von Patentanspruch 1.The invention relates to a device for extracting air for sighting or classifying devices according to the preamble of claim 1.

Sicht- und Klassiervorrichtungen sind Spezialmaschinen, die in großer Anzahl in der Getreidemüllerei verwendet werden. Es werden damit Korn wie auch Mahlgüter in die jeweils gewünschte Fraktion getrennt.Sighting and classifying devices are special machines that are used in large numbers in grain milling. It is used to separate grain as well as regrind into the desired fraction.

In beiden Gattungen bildet ein Arbeitstisch das Herz der Vorrichtung, über den das zu trennende Gut durch eine Vibrationsbewegung gefördert wird. Unterstützt durch eine an die Feinheit des Produktes angepaßte Luftgeschwindigkeit findet eine Trennung des Gutes sowohl nach der Schwere wie auch nach der Größe bzw. nach einem entsprechenden Formfaktor statt. Voraussetzung für eine hohe Trennqualität ist insbesondere eine über die ganze Maschinenlänge kontrollierbare Luftmenge, wozu ein nach oben konisch sich verjüngender Luftverteilraum mit einer Anzahl von etwa 10 bis 20 schottenartig ausgebildeter Luftführungskammern eingesetzt wird. Jeder Luftführungskammer bzw. Schotte wird ein Drosselelement zugeordnet, womit die Luftmenge entsprechend der jeweils gewünschten Trennarbeit einstellbar ist. Vom Luftverteilraum wurde die Luft bisher bei bekannten Maschinen an einer Stelle zentral aspiriert.In both types, a work table forms the heart of the device, through which the material to be separated is conveyed by a vibration movement. Supported by an air velocity that is adapted to the fineness of the product, the goods are separated according to their weight as well as their size or a corresponding form factor. A prerequisite for high separation quality is, in particular, a quantity of air that can be controlled over the entire length of the machine, for which purpose an upwardly tapering air distribution space with a number of approximately 10 to 20 air duct chambers is used. A throttle element is assigned to each air guide chamber or bulkhead, with which the amount of air can be adjusted in accordance with the desired separation work. Up to now, the air has been centrally aspirated at one point in known machines from the air distribution room.

Aus der AU-B-483 698 ist eine Vorrichtung zum Reinigen und Trennen von körnigem Material bekannt, bei der zunächst auf einem Sieb befördertes Material zu Trennzwecken teilweise in einen zyklonartigen Zentrifugalseparator hineingesaugt wird.From AU-B-483 698 a device for cleaning and separating granular material is known, in which material conveyed on a sieve is first partially sucked into a cyclone-type centrifugal separator for separation purposes.

Dieser Zentrifugalseparator weist in seiner Mitte einen quer zur Strömungsrichtung innerhalb des Separators verlaufenden Absaugkanal auf. An der Innenwandung des Zentrifugalseparators geführte Luft sowie leichtere Teilchen können über einzelne Öffnungen in der Außenwand des quer verlaufenden Absaugkanales abgezogen werden. Schwerere Teilchen, die sich gegenüber den leichteren Teilchen im Zentrifugalseparator näher an dessen Innenwand bewegen, werden nach noch nicht vollständigem Umlauf im Zentrifugalseparator zwecks Trennung von den leichteren Bestandteilen an seiner Öffnung in der Außenwand ausgeschieden.This centrifugal separator has in its center a suction channel running transversely to the flow direction within the separator. Air and lighter particles carried on the inner wall of the centrifugal separator can be drawn off via individual openings in the outer wall of the transverse suction channel. Heavier particles, which move closer to the inner wall compared to the lighter particles in the centrifugal separator, are excreted at their opening in the outer wall after separation in the centrifugal separator so that they are not yet completely circulated.

Diese Vorrichtung hat jedoch den Nachteil, daß aufgrund der Kanten der Öffnungen im Absaugkanal, wie aber auch durch die Kanten der Öffnung in der Außenwand des Zentrifugalseparators der homogene Luftstrom gestört wird. Es entstehen an diesen Stellen Luftwirbel, wie aber auch Toträume, in denen sich unerwünscht Material ablagert, was die Strömungseigenschaften innerhalb und damit den Absaug- und Trenneffekt der Vorrichtung insgesamt verschlechtert.However, this device has the disadvantage that the homogeneous air flow is disturbed due to the edges of the openings in the suction channel, but also due to the edges of the opening in the outer wall of the centrifugal separator. At these points, air vortices arise, but also dead spaces in which material is undesirably deposited, which worsens the flow properties within and thus the suction and separation effect of the device as a whole.

Eine ähnliche Vorrichtung ist aus der DE-A- 2 342 091 bekannt, bei der ein etwa um 180° kreisförmig gebogener Umlenksichter ebenfalls in seinem Zentrum einen quer zur Strömungsrichtung im Umlenksichter verlaufenden Abscheidekanal aufweist. Mit dieser Vorrichtung sollen Kohlekörner von an der Oberfläche haftenden staubförmigen Partikeln befreit und die über 0,5 mm liegende Kohlefraktion während der über 180° -igen Umlenkung im Sichter aus der Gasströmung ausgeschleudert und über eine Leitung in eine Setzmaschine ausgetragen werden. Die unter 0,5 mm liegende staubförmige Fraktion wird mit dem Gasstrom durch das am Umlenksichter angeordnete Gasabzugsrohr in einen Staubabscheider abgetragen. Auch bei diesem Gasstrom entstehen Wirbel, wobei zusätzlich zu den schon in der AU-B- 483 698 beschriebenen Nachteilen bezüglich derartiger Wirbelbildungen hinzukommt, daß eine den freien Strömungsquerschnitt verändernde Klappe im Strömungsanfangsbereich des Umlenksichters auf ihrer Rückseite sehr rasch Teilchenablagerungen aufweist, die unmittelbar eine Störung der Funktion dieser Klappe bewirken.A similar device is known from DE-A-2 342 091, in which a deflection sifter which is curved approximately 180 ° in a circular manner also has in its center a separating channel which runs transversely to the flow direction in the deflection sifter. With this device, coal grains are to be freed of dust-like particles adhering to the surface and the coal fraction lying above 0.5 mm is thrown out of the gas flow during the 180 ° deflection in the classifier and discharged via a line into a setting machine. The dust-like fraction below 0.5 mm is removed with the gas flow through the gas exhaust pipe arranged on the deflector into a dust separator. Vortexes also occur in this gas stream, whereby in addition to the disadvantages already described in AU-B-483 698 with regard to vortex formation such as this, a flap which changes the free flow cross section in the flow beginning region of the deflector sifter very quickly has particle deposits which immediately cause a disturbance the function of this valve.

Aus der FR-A- 926 612 schließlich ist ein Absaugkanal bekannt, der teilweise in einer einem Luftverteilraum ähnlichen Haube eingebaut bzw. eingelassen ist. Die angesaugte Luft streicht an beiden Innenseiten des Absaugkanals gegensinnig entlang, und die dadurch gebildeten Luftströmungswirbel eliminieren sich gegenseitig beim jeweiligen Zusammentreffen. An diesen Eliminationsstellen der Luft entstehen schließlich ungewünschte Toträume, die zur ungewünschten Produktablagerungen führen und eine häufige und zeitaufwendige Reinigung erfordern.Finally, from FR-A-926 612 a suction channel is known which is partially installed or embedded in a hood similar to an air distribution space. The sucked-in air sweeps in opposite directions on both inner sides of the suction channel, and the air flow vortices thus formed mutually eliminate each other when they meet. At these points of elimination of the air, undesired dead spaces ultimately arise, which lead to undesired product deposits and require frequent and time-consuming cleaning.

Ausgehend hiervon liegt der Erfindung die Aufgabe zugrunde, bei einfachem Aufbau diese Nachteile möglichst weitgehend zu beheben.Proceeding from this, the object of the invention is to eliminate these disadvantages as far as possible with a simple structure.

Erfindungsgemäß wird dies bei der Vorrichtung der eingangs genannten Art durch die Merkmale des kennzeichnenden Teils von Anspruch 1 gelöst.According to the invention, this is achieved in the device of the type mentioned at the outset by the features of the characterizing part of claim 1.

Durch den tan gentialen Übergang entsteht im Absaugkanal eine Zyklonströmung, die den Vorteil mit sich bringt, daß sich weder Staub noch sonstige Partikel ablagern können. Damit sichert die Erfindung nicht nur eine Reinhaltung der Maschine, sondern verbessert auch deren Betriebssicherheit.The tan gential transition creates a cyclone flow in the suction channel, which has the advantage that neither dust nor other particles can be deposited. The invention thus not only ensures that the machine is kept clean, but also improves its operational safety.

Werden jeder Luftführungskammer jeweils eine Drossel zugeordnet, so bildet sich vorteilhaft im Absaugkanal eine starke Wirbelströmung unabhängig von der Öffnungsstellung der Drosseln aus. Darüberhinaus zeigte sich, daß auch das vollständige schließen einzelner Drosseln weder die Wirbelbildung noch die selbsttätige Reinhaltung des Absaugkanales beeinflußte.If a throttle is assigned to each air guide chamber, a strong vortex flow is advantageously formed in the suction channel regardless of the open position of the throttle. In addition, it was found that even the complete closing of individual throttles did not affect the vortex formation or the automatic cleaning of the suction channel.

Sind Optimalstellungen für die Drosseln einmal gefunden, so können sie bei Wiederholung des gleichen Arbeitsvorganges jederzeit wieder unschwer erfolgreich verwendet werden.Once optimal positions for the chokes have been found, they can easily be used again at any time if the same process is repeated.

In vorteilhafter Ausgestaltung der erfindungsgemäßen Vorrichtung können die Drosseln im Übergangsbereich zwischen Luftverteilraum und Absaugkanal angeordnet werden, wodurch sich nicht nur eine kompakte Bauweise, sondern auch eine günstige Führung der Luftströmung ergibt, da der Übergangsbereich und die Drosseln nur eine einzige gemeinsame Störung in der Luftströmung ausbilden.In an advantageous embodiment of the device according to the invention, the throttles can be arranged in the transition area between the air distribution space and the suction duct, which results not only in a compact design but also in a favorable guidance of the air flow, because the transition area and the throttles form only one common disturbance in the air flow.

Ganz besonders bevorzugt werden die Drosseln als Einstellschieber ausgebildet. Es hat sich gezeigt, daß im Zusammenhang mit dem tangentialen Übergang vom Luftverteilraum in den Absaugkanal Einstellschieber eine sehr genaue und in einem großen Bereich nahezu lineare Verstellung des örtlichen Luftdurchsatzes ermöglichen, da die Umlenkwinkel für die Luftströmung nur geringfügig geändert werden. Bei Vorrichtungen mit weniger großen Anforderungen an die Einstellgenauigkeit der Luftmenge können die Drosselelemente vorzugsweise als Verstellklappen ausgebildet und, in Strömungsrichtung der Luft gesehen, hinter dem Luftverteilraum angeordnet werden.The throttles are very particularly preferably designed as adjusting slides. It has been shown that, in connection with the tangential transition from the air distribution space into the suction channel, adjustment slides allow a very precise and almost linear adjustment of the local air flow rate over a wide range, since the deflection angles for the air flow are changed only slightly. In devices with less stringent requirements for the setting accuracy of the air quantity, the throttle elements can preferably be designed as adjusting flaps and, seen in the direction of flow of the air, can be arranged behind the air distribution space.

Eine weitere, sehr vorteilhafte Ausgestaltung der erfindungsgemäßen Vorrichtung besteht auch darin, daß der Absaugkanal als getrenntes Bauteil ausgebildet und dem Luftverteilraum als liegender Zyklon ("rucksackartig") aufgesetzt ist. Dies erlaubt es einerseits, bei der Gesamtvorrichtung an Bauhöhe einzusparen, gleichzeitig aber auch eine günstige Herstellung, ganz besonders wenn der Absaugkanal einen konstanten Querschnitt aufweist. Bezüglich dieses konstanten Querschnittes konnte in Versuchen gezeigt werden, daß gerade bei schwierigen mehlartigen Gütern, also für die entsprechenden Grießpassagen, so gut wie keine unerwünschten Produktablagerungen mehr festzustellen sind. Sehr vorteilhaft ist es ferner, wenn derAbsaugkanal im Querschnitt wenigstens teilweise gerundet, vorzugsweise kreisförmig ausgebildet ist. Als besonders günstig hat es sich weiterhin gezeigt, wenn der Durchmesser des Querschnitts des Absaugkanales etwa ein Drittel bis ein Viertel der Breite der Sieblagen beträgt.A further, very advantageous embodiment of the device according to the invention also consists in the suction channel being designed as a separate component and the air distribution space being placed as a lying cyclone (“backpack-like”). On the one hand, this makes it possible to save on the overall height of the overall device, but at the same time it is also inexpensive to manufacture, particularly if the suction channel has a constant cross section. With regard to this constant cross-section, tests have shown that, especially with difficult flour-like goods, ie for the corresponding semolina passages, there is virtually no longer any undesirable product deposits. It is also very advantageous if the suction channel is at least partially rounded in cross section, preferably circular. It has also proven to be particularly favorable if the diameter of the cross section of the suction channel is approximately one third to one fourth the width of the sieve layers.

Die Erfindung wird nachfolgend anhand der Zeichnung im Prinzip beispielshalber noch näher erläutert. Es zeigen:

  • Fig. 1 eine Längsansicht einer Grießputzmaschine mit einer erfindungsgemäßen Absaugvorrichtung;
  • Fig. 2 den Schnitt 11-11 aus Fig. 1;
  • Fig. 3 eine schematische Darstellung des oberen Luftverteilraumes mit Absaugkanal und Klappenverstellung bei einer erfindungsgemäßen Vorrichtung;
  • Fig. 4 eine Schnittdarstellung längs IV-IV in Fig. 3;
  • Fig. 5 eine zur Darstellung nach Fig. 3 geänderte weitere Ausführungsform einer erfindungsgemäßen Vorrichtung mit Schieberverstellung, sowie
  • Fig. 6 eine Detail-Draufsicht auf die in Fig. 5 dargestellte Vorrichtung.
The invention is explained in more detail below in principle by way of example with reference to the drawing. Show it:
  • Figure 1 is a longitudinal view of a semolina cleaning machine with a suction device according to the invention.
  • FIG. 2 shows the section 11-11 from FIG. 1;
  • Figure 3 is a schematic representation of the upper air distribution space with suction channel and flap adjustment in a device according to the invention.
  • Fig. 4 is a sectional view along IV-IV in Fig. 3;
  • 5 shows a further embodiment of a device according to the invention with slide adjustment modified as shown in FIG. 3, and
  • Fig. 6 is a detailed top view of the device shown in Fig. 5.

Zunächst sei auf die Fig. 1 und 2 Bezug genommmen, in denen eine sogenannte "Doppelmaschine" dargestellt ist, die aus zwei arbeitstechnisch vollständig getrennten Grießputzmaschinen besteht, wie dies in Fig. 2 gezeigt ist. Diese beiden Grießputzmaschinen sind links und rechts bezüglich einer mittleren Ständerkonstruktion getrennt angeordnet.First of all, reference should be made to FIGS. 1 and 2, in which a so-called “double machine” is shown, which consists of two semolina cleaning machines that are completely separate in terms of working technology, as shown in FIG. 2. These two semolina cleaning machines are arranged on the left and right with respect to a central stand construction.

In Fig. 1 erkennt man links oben einen Einlauf 1 für das der Vorrichtung, zuzuführende Produkt und rechts unten Ausläufe 2 für den Siebabstoß. Des weiteren sind drei übereinander angeordnete Sieblagen 3 vorgesehen, wobei unter diesen eine innere Auffangvorrichtung 4 sowie eine äußere Auffangvorrichtung 5 angeordnet sind (Fig. 2), in denen der Siebdurchfall gesammelt wird. Dabei weist in der Regel jede einzelne Auffangvorrichtung 4 bzw. 5 zwei Abläufe 6 bzw. 7 auf. Die Sieblagen 3 sind je zu einem Putzkasten 8 vereinigt (Fig. 2), so daß jedem Putzkasten 8 entsprechend der dargestellten Ausführungsform zwei Ausläufe 2 für den Siebabstoß sowie vier Abläufe 6 und 7 für den Siebdurchfall zugeordnet sind. Jeder Putzkasten 8 ist über eine Endstütze 12 (Fig. 1) über Schwingelemente bzw. Gummihohlfedern 13 an einem Ständerfuß 10 eines Ständers 9 schwingfähig abgestützt. Mit der Endstütze 12 ist ein Unwuchterreger 14 fest verbunden, dessen Stoßrichtung (vgl. Pfeil 15 in Fig. 1) durch eine Verdrehung des Unmwuchterregers 14 an einer rohrförmigen Querverbindung 16 einstellbar ist. Ebenso läßt sich, was bekannt ist, die Stärke der Unwuchtkräfte durch entsprechende Einstellung der Unwuchtgewichte 17 regulieren. An der Querverbindung 16 sind zwei Unwuchterreger 14 befestigt und elektrisch so angeschlossen, daß sie gegenläufig drehen. Damit heben sich ihre seitlichen Unwuchtkomponeten auf und es entsteht eine rein lineare Längsschwingung in Richtung des Pfeiles 15. Über den Unwuchterregern 14 ist eine Abdekkung 18 angebracht, die zur baulichen Vereinfachung als Teil des schwingenden Systems ausgebildet ist.1 shows an inlet 1 at the top left for the product to be supplied to the device and outlet 2 at the bottom right for the screen rejection. Furthermore, three screen layers 3 arranged one above the other are provided, an inner collecting device 4 and an outer collecting device 5 being arranged beneath them (FIG. 2), in which the sieve diarrhea is collected. As a rule, each individual collecting device 4 or 5 has two processes 6 or 7. The sieve layers 3 are each combined to form a cleaning box 8 (FIG. 2), so that each cleaning box 8 is assigned two outlets 2 for the screen rejection and four outlets 6 and 7 for the screen diarrhea in accordance with the illustrated embodiment. Each cleaning box 8 is supported by an end support 12 (FIG. 1) via oscillating elements or hollow rubber springs 13 on a stand base 10 of a stand 9 so that it can vibrate. An unbalance exciter 14 is fixedly connected to the end support 12, the direction of impact (cf. arrow 15 in FIG. 1) can be adjusted by rotating the unbalance exciter 14 on a tubular cross connection 16. Likewise, what is known can regulate the strength of the unbalance forces by appropriate adjustment of the unbalance weights 17. At the cross connection 16, two unbalance exciters 14 are attached and electrically connected so that they rotate in opposite directions. This eliminates their lateral unbalance components and there is a purely linear longitudinal vibration in the direction of arrow 15. A cover 18 is attached above the unbalance exciters 14, which is designed as part of the vibrating system for structural simplification.

Die Auffangvorrichtung 4 ist als Schwingförderrinne ausgebildet, die auf beiden Endseiten auf je einer in Gummi gelagerten Stütze 19 ruht (Fig. 1). Der Schwingantrieb der Auffangvorrichtung 4 erfolgt über einen Hebel 20, der die schwingende Endstütze 12 mit der Stütze 19 verbindet. Je nach Höhenlage des Angriffspunktes des Hebels 20 an der Stütze 19 (diese Höhenlage ist einstellbar) kann somit der Schwinghub der Auffangvorrichtung 4 unabhängig vom Schwinghub des Putzkastens 8 gewählt bzw. eingestellt werden. Der Ständer 9 trägt direkt alle nicht-schwingenden Bauteile, wobei über dem Ständerunterteil die schwingenden Elemente gelagert sind. Der Ständer 9 weist weiterhin auf beiden Endseiten je eine vertikale Stütze 21 auf (Fig. 2), die unten über eine Erweiterung in eine Fußkonstruktion übergeht. Gemäß der Darstellung der Fig. 2 reicht die vertikale Stütze 21 ein wenig über die oberste Sieblage hinaus und trägt den Ständerkopf 11, der im wesentlichen den oberen Luftverteilraum 22 ausbildet. Dieser obere Luftverteilraum 22 weist eine nach oben verjüngte Form auf und ist über seine Länge durch Schotten 23 in sechzehn getrennte Luftführungskammern 24 aufgeteilt. Die Schotten 23 sind, wie aus Fig. 1 ersichtlich, bis nahe an die oberste Sieblage geführt, wobei der Abstand so gewählt ist, daß er etwas größer ist als die größte jemals sich einstellende Schichtdicke "S" des Gutes (vgl. Fig. 3 und Fig. 5).The collecting device 4 is designed as a vibrating conveyor trough, which rests on both end sides on a support 19 mounted in rubber (FIG. 1). The oscillation drive of the collecting device 4 takes place via a lever 20 which connects the oscillating end support 12 to the support 19. Depending on the height of the point of application of the lever 20 on the support 19 (this height can be adjusted), the swing stroke of the collecting device 4 can thus be selected or adjusted independently of the swing stroke of the cleaning box 8. The stand 9 carries all non-vibrating components directly, the vibrating elements being mounted above the lower part of the stand. The stand 9 also has a vertical support 21 on each end side (FIG. 2), which merges into a foot construction at the bottom via an extension. According to the illustration in FIG. 2, the vertical support 21 extends a little beyond the uppermost sieve position and supports the stand head 11, which essentially forms the upper air distribution space 22. This upper air distribution chamber 22 has a tapered shape and is upwardly g over its length by bulkheads 23 into sixteen separate Luftführun skammern 24 divided. The bulkheads 23, as can be seen in FIG. 1, are brought close to the uppermost sieve layer, the distance being chosen so that it is somewhat larger than the greatest layer thickness "S" of the material which ever occurs (see FIG. 3 and Fig. 5).

Die oberen Schrägflächen des Luftverteilraumes 22 weisen über ihre ganze Länge durchsichtige Fenster 25 (Fig. 2) auf, so daß mit einer elektrischen Lichtquelle von der Außenseite der Vorrichtung her das Fließverhalten des Gutes über der obersten Sieblage 3 kontrolliert werden kann. In den Fig. 3 und 4 erkennt man zwischen dem oberen Ende des Luftverteilraumes 22 und einem auf dem Luftverteilraum 22 sitzenden. Absaugsammelkanal 27 Drosseln in Form von Verstellklappen 28, die einzeln über einen Kopf 29 dem jeweiligen Luftbedarf entsprechend eingestellt werden können. Dabei schließen, wie die Fig. 3 bis 6 zeigen, die Innenwandungen von Luftverteilraum und Absaugkanal in einem Übergangsbereich so aneinander an, daß die Luft tangential in den Absaugkanal übergeht, so daß sich im Absaugkanal eine Zyklonströmung ausbildet.The upper inclined surfaces of the air distribution space 22 have transparent windows 25 over their entire length (FIG. 2), so that the flow behavior of the material over the top sieve layer 3 can be controlled with an electric light source from the outside of the device. 3 and 4 can be seen between the upper end of the air distribution space 22 and one sitting on the air distribution space 22. Suction manifold 27 throttles in the form of adjusting flaps 28, which can be individually adjusted according to the respective air requirement via a head 29. 3 to 6 show, the inner walls of the air distribution space and the suction duct adjoin one another in a transition area such that the air passes tangentially into the suction duct, so that a cyclone flow forms in the suction duct.

Bei der Inbetriebnahme der gezeigten Grießputzmaschine wird der Vibrator 14 eingeschaltet so daß der Putzkasten 8, der Boden 32 und die Auffangvorrichtungen 4 und 5 die vorgewählte Schwingbewegung in Längsrichtung der Vorrichtung durchführen. Ebenso wird die ganze Vorrichtung über den Absaugsammelkanal 27 bzw. eine damit verbundene Aspiration in geringen Unterdruck versetzt. Je nach Trennaufgabe werden alle Schieber und Klappen 28 provisorisch eingestellt, wonach das Produkt in den Einlauf 1 eingespeist werden kann. Das Produkt fällt sofort auf die oberste Sieblage 3. Durch die Schüttelbewegung, die dem Gut auifgeprägt wird, sowie durch die bewußt vom Einlauf 1 zum Auslauf 2 schräg nach unten geneigten Sieblagen und durch die Luftströmung durch die Sieblagen 3 verhält sich das Produkt flüssigkeitsähnlich (fluidisiert). Die zentrale Aufgabe der Grießputzmschine liegt im eigentlichen Siebvorgang. Also darf die Luftströmung nicht so stark eingestellt werden, daß die ganze Produktschicht von den Sieblagen abgehoben werden könnte. Vielmehr dient die Luft in erster Linie der Funktion, das produkt aufzulokkern und gleichmäßig über die ganze Fläche zu verteilen.When the semolina cleaning machine shown is started up, the vibrator 14 is switched on so that the cleaning box 8, the bottom 32 and the collecting devices 4 and 5 carry out the preselected oscillating movement in the longitudinal direction of the device. Likewise, the entire device is placed in a slight negative pressure via the suction collecting duct 27 or an aspiration associated therewith. Depending on the separation task, all slides and flaps 28 are provisionally adjusted, after which the product can be fed into the inlet 1. The product immediately falls on the top sieve layer 3. Due to the shaking movement which is imprinted on the material, as well as the sieve layers deliberately inclined downwards from the inlet 1 to the outlet 2 and the air flow through the sieve layers 3, the product behaves like a liquid (fluidized ). The central task of the semolina cleaning machine lies in the actual sieving process. So the air flow must not be adjusted so much that the entire product layer could be lifted off the sieve layers. Rather, the air primarily serves the function of locating the product and distributing it evenly over the entire surface.

Je nach Aufgabenstellung wird gefordert, daß das Produkt in grobe, mittlere und feine Grieße oder in Kochgrieße und mittlere Grieße usw. fraktioniert werden soll. Im zweiten Fall z. B. können die ersten sechs Schurren 34 in die Auffangvorrichtung 4, die nachfolgenden elf Schurren 34 in die Auffangvorrichtung 5 gerichtet werden. In diesem Fall handelt es sich bei den beiden Siebdurchgängen um Fertigprodukte, die zu den entsprechenden Lagerzellen bzw. zu den Verbrauchern abgegeben werden können. Die Siebabstöße bei den Ausläufen 2 werden teilweise einer nochmaligen Vermahlung oder Zerkleinerung zugeführt und gelangen dann auf eine zweite entsprechend eingestellte Grießputzmaschine.Depending on the task, it is required that the product should be fractionated into coarse, medium and fine size or into cooking size and medium size etc. In the second case, e.g. B. the first six chutes 34 can be directed into the collecting device 4, the subsequent eleven chutes 34 into the collecting device 5. In this case, the two sieve passes are finished products that can be delivered to the corresponding storage cells or to the consumers. The screen rejects at the outlets 2 are partially re-ground or comminuted and then reach a second, appropriately set, semolina cleaning machine.

In jeder Grießputzmaschine müssen die spezifischen, für die jeweilige Aufgabe geeigneten Siebmaschenweiten gewählt werden.The specific sieve mesh sizes suitable for the respective task must be selected in each semolina cleaning machine.

Ist die Grießputzmaschine einmal in vollem Betrieb, so beginnt die eigentliche Aufgabe des Müllers, nämlich die Beurteilung der Arbeitsweise der Vorrichtung sowie die mengenmäßige und qualitative Beurteilung der gewonnenen Fraktionen.Once the semolina cleaning machine is in full operation, the miller's actual task begins, namely the assessment of the functioning of the device and the quantitative and qualitative assessment of the fractions obtained.

Hierzu wird die Lichtquelle 26 (Fig. 2) eingeschaltet, so daß der ganze Raum innerhalb des Luftverteilraumes 22 ausgeleuchtet ist. Durch die Fenster 25 kann über die ganze Länge das Fließverhalten des produktes innerhalb der einzelnen Luftführungskammern 24 beobachtet werden. Zeigt sich innerhalb einer oder mehrerer Luftführungskammern 24 ein Bild ähnlich dem kochenden Wassers, so wird die Luftmenge in den betreffenden Luftführungskammern 24 über die Verstellklappen 28 gedrosselt. Umgekehrt kann aber auch an einzelnen Stellen ein Stau entstchen: hier muß dann die örtliche Luftmenge sinngemäß erhöht werden. Ist das Fließverhalten des Produktes einwandfrei und sind im Mischprodukt (Ausläufe) keine Anteile vorhanden, die zum Siebdurchfall gehören, so wird die Qualität der Siebdurchfälle nochmals überprüft und die Einstellung der Schurren 34 auf die jeweils richtigen Auffangvorrichtungen 4 bzw. 5 vorgenommen.For this purpose, the light source 26 (FIG. 2) is switched on, so that the entire space within the air distribution space 22 is illuminated. The flow behavior of the product within the individual air guide chambers 24 can be observed through the windows 25 over the entire length. If an image similar to the boiling water appears in one or more air guiding chambers 24, the amount of air in the relevant air guiding chambers 24 is throttled via the adjustment flaps 28. Conversely, a jam can also occur at individual points: here the local air volume must be increased accordingly. If the flow behavior of the product is flawless and if there are no parts in the mixed product (outlets) that belong to sieve diarrhea, the quality of the sieve diarrhea is checked again and the chutes 34 are adjusted to the correct collecting devices 4 and 5, respectively.

Wie aus Fig. 1 ersichtlich ist, können von jeder Auffangvorrichtung 4 bzw. 5 je zwei verschiedene Abläufe 6 bzw. 7 gewählt werden, so daß von jedem Putzkasten 8 vier verschiedene Fraktionen separiert werden können. Dabei nimmt der Querschnitt des Absaugkanales 27 in Richtung der Luftströmung zu.As can be seen from FIG. 1, two different processes 6 and 7 can be selected from each collecting device 4 or 5, so that four different fractions can be separated from each cleaning box 8. The cross section of the suction channel 27 increases in the direction of the air flow.

Die Fig. 5 und 6 zeigen, alternativ zu den Fig. 3 und 4, eine weitere vorteilhafte Ausführungsform. Anstelle der dort verwendeten Verstellklappen 28 sind bei der Lösung der Fig. 5 und 6 Schieber 40 eingesetzt. Diese Schieber 40 erlauben eine genauere Einstellung des Luftbedarfes in allen Schieberstellungen. Entsprechend den Umdrehungen des Kopfes 29 wird eine proportionale Querschnittsveränderung der Schieberöffnung verursacht. Wäre statt eines Schiebers 40 eine Klappe 28 eingesetzt, würde hier bei einer Verstellung demgegenüber keine ähnliche, proportionale Querschnittsveränderung mehr eintreten, da sich in einem solchen Fall der wirksame Öffnungsquerschnitt nicht mehr proportional zur Umdrehung des Kopfes 29 ändern würde. Die Schieberlösung hat zudem den weiteren Vorteil, daß der freie Querschnitt des Absaugsammelkanales 27 durch die verschiedenen Öffnungsstellungen der Schieber 40 nicht beeinflußt wird.5 and 6 show, as an alternative to FIGS. 3 and 4, a further advantageous embodiment. Instead of the adjustment flaps 28 used there, sliders 40 are used in the solution of FIGS. 5 and 6. These sliders 40 allow more precise adjustment of the air requirement in all slider positions. A proportional change in cross-section of the slide opening is caused in accordance with the revolutions of the head 29. If a flap 28 were used instead of a slider 40, no similar, proportional cross-sectional change would occur in this case, however, since in such a case the effective opening cross-section would no longer change in proportion to the rotation of the head 29. The slide solution also has the further advantage that the free cross section of the suction collecting duct 27 is not influenced by the different open positions of the slide 40.

Besonders bei der Lösung gemäß den Fig. 5 und 6 hat es sich gezeigt, daß der Absaugsammelkanal 27 in Luftströmungsrichtung mit konstantem Querschnitt ausgeführt sein kann. Entsprechende Praxisversuche haben gezeigt, daß die erfindungsgemäße Absaugvorrichtung insbesondere auch bei Trennvorrichtungen, die primär nach der Schwere arbeiten, wie auch bei verschiedenen Ausführungen von Leichtkornauslesern und auch bei kombinierten Maschinen verwendet werden kann. Von den genannten Maschinen werden stets Arbeitsprozesse ausgeführt, bei denen größere Arbeitsflächen in eine Mehrzahl kleiner, in der Luftmenge kontrollierbare Flächenabschnitte eingeteilt werden müssen, wobei jedoch eine Steuerung der Luftmenge nur oberhalb der Schüttschicht (in aller Regel auf der Saugseite) möglich sein muß. Damit erhält man eine gute Steuerbarkeit der Luftmenge für den Saugbetrieb ohne die Nachteile, die beim Stande der Technik gerade durch starke Verstaubung entsprechender Drosselkanäle oft eintreten.5 and 6, in particular, it has been shown that the suction collecting duct 27 can be designed with a constant cross section in the air flow direction. Corresponding practical tests have shown that the suction device according to the invention can also be used in particular in separation devices which primarily work according to their weight, as well as in different versions of light-grain readers and also in combined machines. Work processes are always carried out by the machines mentioned, in which larger work surfaces in a plurality smaller, controllable areas of the air volume must be divided, but it must be possible to control the air volume only above the bed layer (usually on the suction side). This gives good controllability of the air volume for suction operation without the disadvantages that often occur in the prior art due to the strong dusting of the corresponding throttle ducts.

Claims (8)

1. Device for the extraction of air for separating or grading machines, having an air distribution chamber (22) above the screen layers (3), which has a multiplicity of air circulation chambers (24) formed by partitions, and to whose upper region a suction channel (27) extending over its entire length is connected, characterized in that the inside walls of air distribution chamber (22) and suction channel (27) connect to each other in a transition region in such a way that the air passes tangentially into the suction channel (27), so that a cyclone flow forms in the suction channel (27).
2. Device according to Claim 1, characterized in that a throttle (28) is allocated to each air circulation chamber (24).
3. Device according to Claim 2, characterized in that the throttles (28) are disposed in the transition region between the air distribution chamber (22) and the suction channel (27).
4. Device according to Claim 2 or 3, characterized in that the throttles are designed in the form of adjusting slides (40).
5. Device according to Claim 2 or 3, characterized in that the throttles are designed as adjusting flaps (28) and, viewed in the direction of flow of the air, are disposed downstream of the air distribution chamber (22).
6. Device according to one of Claims 1 to 5, characterized in that the suction channel (27) is designed as a separate component and is placed on the air distribution chamber (22) as a horizontal cyclone.
7. Device according to one of Claims 1 to 6, characterized in that the suction channel (27) has a constant cross-section.
8. Device according to one of Claims 1 to 7, characterized in that the suction channel (27) has a round, preferably circular cross-section.
EP85102170A 1984-03-22 1985-02-27 Air suction device for a sifting or sorting apparatus Expired - Lifetime EP0155556B1 (en)

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AT85102170T ATE56158T1 (en) 1984-03-22 1985-02-27 DEVICE FOR SUCTIONING AIR FROM CLASSIFIERS OR CLASSIFIERS.

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DE3410573 1984-03-22
DE3410573A DE3410573C2 (en) 1984-03-22 1984-03-22 Device for cleaning semolina

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EP0155556A2 EP0155556A2 (en) 1985-09-25
EP0155556A3 EP0155556A3 (en) 1987-06-24
EP0155556B1 true EP0155556B1 (en) 1990-09-05

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EP85101898A Expired EP0155527B1 (en) 1984-03-22 1985-02-21 Device for cleaning semolina
EP85101992A Expired EP0155537B1 (en) 1984-03-22 1985-02-22 Device for cleaning semolina
EP85102170A Expired - Lifetime EP0155556B1 (en) 1984-03-22 1985-02-27 Air suction device for a sifting or sorting apparatus

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EP85101898A Expired EP0155527B1 (en) 1984-03-22 1985-02-21 Device for cleaning semolina
EP85101992A Expired EP0155537B1 (en) 1984-03-22 1985-02-22 Device for cleaning semolina

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EP (3) EP0155527B1 (en)
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DE (4) DE3410573C2 (en)
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101850335A (en) * 2009-03-31 2010-10-06 株式会社佐竹 Purifier
EP2236219A3 (en) * 2009-03-31 2013-04-17 Satake Corporation Purifier
CN101850335B (en) * 2009-03-31 2014-05-21 株式会社佐竹 Purifier

Also Published As

Publication number Publication date
US4806235A (en) 1989-02-21
DE3564659D1 (en) 1988-10-06
SU1477238A3 (en) 1989-04-30
EP0155527B1 (en) 1988-08-31
DE3410573C2 (en) 1986-03-13
DE3560153D1 (en) 1987-06-11
JPS60255181A (en) 1985-12-16
JPS60216872A (en) 1985-10-30
US4636305A (en) 1987-01-13
EP0155556A2 (en) 1985-09-25
EP0155527A2 (en) 1985-09-25
EP0155537A2 (en) 1985-09-25
DE3410573A1 (en) 1985-10-03
ATE56158T1 (en) 1990-09-15
KR890004600B1 (en) 1989-11-20
JPH0113916B2 (en) 1989-03-08
DE3579482D1 (en) 1990-10-11
ES541472A0 (en) 1986-05-16
EP0155537A3 (en) 1986-02-05
KR850006866A (en) 1985-10-21
EP0155556A3 (en) 1987-06-24
EP0155537B1 (en) 1987-05-06
ATE26932T1 (en) 1987-05-15
JPH0122827B2 (en) 1989-04-27
JPH0113917B2 (en) 1989-03-08
ES8606797A1 (en) 1986-05-16
ATE36817T1 (en) 1988-09-15
JPS60220175A (en) 1985-11-02
EP0155527A3 (en) 1986-02-05

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