EP3099426B1 - Separator with a bypass - Google Patents
Separator with a bypass Download PDFInfo
- Publication number
- EP3099426B1 EP3099426B1 EP15703729.2A EP15703729A EP3099426B1 EP 3099426 B1 EP3099426 B1 EP 3099426B1 EP 15703729 A EP15703729 A EP 15703729A EP 3099426 B1 EP3099426 B1 EP 3099426B1
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- European Patent Office
- Prior art keywords
- fine
- separation
- classifier
- separator according
- stock
- Prior art date
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- 238000009423 ventilation Methods 0.000 claims description 29
- 238000005192 partition Methods 0.000 claims description 24
- 238000000926 separation method Methods 0.000 claims description 18
- 230000001419 dependent effect Effects 0.000 claims 2
- 239000000463 material Substances 0.000 description 110
- 230000003068 static effect Effects 0.000 description 53
- 230000000007 visual effect Effects 0.000 description 12
- 239000002245 particle Substances 0.000 description 11
- 230000000694 effects Effects 0.000 description 8
- 238000011144 upstream manufacturing Methods 0.000 description 5
- 238000009826 distribution Methods 0.000 description 3
- 241000196324 Embryophyta Species 0.000 description 2
- 239000013590 bulk material Substances 0.000 description 2
- 230000001276 controlling effect Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 241000237858 Gastropoda Species 0.000 description 1
- 240000001439 Opuntia Species 0.000 description 1
- 235000004727 Opuntia ficus indica Nutrition 0.000 description 1
- 241000209504 Poaceae Species 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000003306 harvesting Methods 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 238000009827 uniform distribution Methods 0.000 description 1
Images
Classifications
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- 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
- B07B9/00—Combinations of apparatus for screening or sifting or for separating solids from solids using gas currents; General arrangement of plant, e.g. flow sheets
- B07B9/02—Combinations of similar or different apparatus for separating solids from solids using gas currents
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- 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
- B07B4/00—Separating solids from solids by subjecting their mixture to gas currents
- B07B4/02—Separating solids from solids by subjecting their mixture to gas currents while the mixtures fall
-
- 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
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C13/00—Disintegrating by mills having rotary beater elements ; Hammer mills
- B02C13/14—Disintegrating by mills having rotary beater elements ; Hammer mills with vertical rotor shaft, e.g. combined with sifting devices
Definitions
- the invention relates to a classifier according to the preamble of patent claim 1, with a housing which forms a classifying chamber, in which one or more ventilation floors are arranged and in which classifying gas is flowed through in order to separate fine material from coarse material, a classifying gas inlet and a Visible material inlet opens into the viewing area and a fine goods outlet and a coarse material outlet emerge from the viewing area.
- Such classifiers which are also referred to as statically operating, serve to separate bulk materials into two fractions with different particle size distributions.
- the fractions are separated in the classifying chamber in which the classifying gas flows through the classifying gas in the transverse direction from the classifying material inlet in the direction of the coarse material outlet. Smaller particles are entrained by the sight gas flow and transported to the fine material outlet, while larger particles are discharged through the coarse material outlet.
- the ventilation floors of a static classifier are aligned more or less transversely to the direction of movement of the material to be viewed, with a step-like arrangement of the ventilation floors being often provided ( DE 43 37 215 A1 ).
- an essentially flat ventilation floor is provided with a plurality of ventilation slots.
- the ventilation floor can be composed of a large number of individually interchangeable slotted plates.
- the visible material falling in the visual space hits the ventilation floor or floors and the visual gas flows through there.
- the impact of the material to be sighted on the ventilation floor (s) can, on the one hand, increase the length of time of the material to be placed in the viewing space.
- the impact of the visible material on the ventilation floors causes deagglomeration of frequently present visual material agglomerates, the so-called Schülpen. Both improve the sighting effect of a static classifier.
- Static classifiers are often combined with dynamic classifiers, with the static classifiers regularly being upstream as a coarse classifier and serving as a fine classifier.
- Dynamic classifiers are based on one Separation of two fractions of the material to be classified, which differ in terms of particle size distribution, by means of a rotating driven basket.
- a combination of a static classifier as a coarse classifier and a dynamic classifier as a fine classifier in a circulation grinding plant for cement clinker is, for example, from the DE 43 37215 A1 known.
- the static sifter is connected downstream of a roller press and is subjected to comparatively coarse and a large number of slugs.
- the coarse material separated in the static classifier is returned to the roller press, while the fine material is fed to a tube mill by means of the classifying gas stream, in which it is further comminuted.
- the material to be viewed is then fed from the tube mill to the dynamic classifier, in which the material to be separated is separated into medium and fine material.
- the very fine material is then removed as finished product from the classifying gas in a separator, while the medium fine material is returned to the tube mill.
- the circulation grinding plant according to the DE 43 37 215 A1 the static sifter and the dynamic sifter are separated both spatially and functionally by the interposition of the tube mill.
- the static classifier thus essentially serves to avoid the supply of excessively large particles or flakes to the tube mill.
- FIG DE 10 2011 055 762 A1 A device for classifying bulk material, in which a static classifier and a dynamic classifier are connected in series in a common housing and thus flowed through by the same classifying gas flow, is shown in FIG DE 10 2011 055 762 A1 known.
- the upstream connection of the static classifier essentially serves to avoid exposure of the rotatingly driven and comparatively sensitive viewing basket of the dynamic classifier to large particles and flakes.
- a dynamic classifier in the housing of which a bypass channel is integrated which bypasses the classifying chamber and via which a part of the dust-air mixture supplied via an inlet can be guided in the classifying room to avoid classifying. This should make it possible to specifically influence the particle sizes in the finished product leaving the dynamic classifier.
- the CA 2 400 859 A1 discloses a device according to the preamble of claim 1, for separating a harvest mixture consisting of grain, chaff and grasses into its components, the device combining a sifter with a cyclone separator.
- the US 2013/0032513 A1 describes a device by means of which a bulk material can both be dried and simultaneously separated into a coarse material fraction and a fine material fraction.
- the object of the invention was to provide a possibility of making the sighting effect of a static classifier changeable in the simplest possible way.
- the invention is based on the one hand on the idea that the volume flow of the sight gas guided through the static classifier represents a control variable which can be easily influenced, the change of which has a relevant effect on the Sighting effect of the sifter.
- the particle size distributions of the material discharged from the static classifier on the one hand as fine material and on the other hand as coarse material can be adjusted by changing the volume flow of the classifying gas. This can be done, in particular, depending on the aggregates downstream of the static classifier (for example a mill or a dynamic classifier).
- a change in the drying effect of the (possibly heated) sight gas can also be achieved by adjusting the volume flow.
- the volume flow of the sight gas could in principle be adjusted to the intended sighting effect by correspondingly controlling a blower generating the sight gas flow.
- the volume flow of the classifying gas for an aggregate downstream of the static classifier, in particular a dynamic classifier is also changed.
- the invention provides, on the one hand, for the volume flow of the sight gas supplied to the static classifier, which can preferably be air, to be regulated in such a way that at least one bypass channel is provided, via which part of the sight gas flow is applied is led past the visual space.
- a generic static classifier which has at least one housing in which the visual space is located, in which one or more ventilation shelves are arranged and in the classifying material of classifying gas, in order to separate the classifying material into fine and coarse material, whereby (at least ) a classifying gas inlet and (at least) one classifying material inlet lead into the classifying room and (at least) one fine material outlet and (at least) one coarse material class exit from the classifying room, characterized by at least one bypass channel integrated in the housing for bypassing the classifying room, the bypass channel going out in the classifying gas inlet and flows downstream of the visual space.
- a viewing space is understood in particular to mean the area of the sifter in which material sifting, that is to say a separation of material, is more specific Grain size is done.
- the material of coarser grain size leaves the visible space through the coarse material outlet, the material of finer grain size entering the fine material outlet.
- the fine material outlet is arranged downstream of the visual space and is designed in such a way that no material is viewed in it.
- the bypass channel opens into the classifier downstream of the classifying space, the bypass channel opening, for example, into the fine material outlet or into a gas inlet of a second, in particular dynamic, classifier downstream of the first classifier.
- a bypass duct integrated into the housing is understood to mean that at least one (preferably all) wall surface delimiting the bypass duct, preferably extending over the entire length of the bypass duct, is part of the housing and thus, in addition to the function of delimiting the bypass duct, structurally (as a supporting wall) or used functionally (e.g. to guide a medium) for other parts of the classifier.
- one or more advantages can be generated compared to an externally running bypass channel, which can be designed, for example, in the form of a bypass hose.
- an externally running bypass channel which can be designed, for example, in the form of a bypass hose.
- Compensators which may be necessary in an external bypass duct to compensate for different thermal expansions, can also be omitted in a bypass duct integrated in the housing.
- a classifier according to the invention that it integrates a static coarse classifier and a fine classifier downstream of it in a housing. Accordingly, it is provided that a second, in particular dynamic, classifier with a second classroom is connected to the fine material outlet, a housing forming the second classifier, which forms the second classroom surrounds, forms a medium fine material outlet and a fine material outlet.
- the fine classifier is a dynamic fine classifier, which accordingly comprises a rotatingly driven classifying rotor arranged in the second classifying chamber, for example in the form of a conventional classifying basket.
- Such a sifter which comprises a static coarse sifter and a fine sifter connected downstream of it, can preferably be used in combination with (at least) one blower used for both (partial) sifters to generate the sifting gas flow.
- the ability to influence the volume flow of the sighting gas through the bypass duct through the static coarse sifter has advantages in particular in the case of such a combination with a fine sifter, since in this way the volume flow through the static coarse sifter can be largely regulated independently of the volume flow through the fine sifter.
- a control element can preferably be provided, by means of which the free flow cross section of the bypass channel can be changed (manually or automatically).
- the control element can be designed, for example, as a control flap or control slide adjustable by means of an actuator.
- the bypass channel forms a plurality of (spatially separated) flow channels.
- bypass channel it can then be provided, in order to even out the partial flows of the sight gas that are conducted via the individual flow channels, that a control element is provided for several and in particular all of the flow channels. It can also be provided that the control elements can be adjusted separately.
- the flow channels end at a distance from the mouth of the bypass channel into the fine material outlet.
- a combination of the partial flows of the sight gas conducted via the flow channels can be particularly advantageous if the sight gas flow conducted through the bypass channel is introduced into the fine material outlet via a relatively small mouth opening in the area of the mouth of the bypass channel compared to the cross-sectional dimensions of the fine material outlet.
- the bypass channel opens decentrally into the fine material outlet, whereby a swirl of the re-mixed total flow of the visible gas can be generated by means of the sight gas flow entering the fine material outlet, which in particular has a positive effect on the visual effect of the static coarse sifter downstream, dynamic fine classifier.
- the direction of rotation of the swirl corresponds to the sight gas flow of the direction of rotation of the sight rotor of the dynamic fine classifier.
- “Decentralized” is understood here to mean that the (middle) flow direction of the sight gas flow entering the fine material outlet from the bypass duct (and in particular the central longitudinal axis of the mouth opening) is the central longitudinal axis of the Cross-sectional areas of the fine material outlet in the area of the mouth of the bypass channel do not intersect.
- the sight gas flow entering the fine material outlet from the bypass channel is introduced as far as possible from the central longitudinal axis and thus as close as possible to a wall of the housing delimiting the fine material outlet.
- the classifier according to the invention has at least two bypass channels, which can preferably be arranged on opposite sides of the first classifying room, for an increased swirl effect the sight gas flows entering the fine material outlet from the two bypass channels can be provided that these two bypass channels are not only decentralized but also open diametrically to each other with respect to a central longitudinal axis of the fine material outlet in the fine material outlet.
- At least one intermediate wall arranged in the fine material outlet and oriented transversely to the ventilation floor or floors can be provided.
- the intermediate wall can stiffen the housing.
- an increase in the load-bearing capacity for the main flow as a result of an increase in the Froude number can be achieved by the at least one intermediate wall, which divides the flow space formed by the fine material outlet for the main flow of the sighting gas into a plurality of partial flow spaces.
- the partition does not hinder the introduction of the sight gas flow conducted through the at least one bypass duct, it can preferably be provided that the bypass duct opens into the fine material outlet downstream of the partition.
- the bypass duct is at a (as large as possible) distance in front of the ventilation plate (s) from the sight gas inlet goes off. This can be implemented in a structurally simple manner by providing a partition wall that extends the bypass channel into the sight gas inlet.
- the Indian Fig. 1 The classifier shown comprises a static coarse classifier 1 and a dynamic fine classifier 2 directly downstream of it. Both are integrated in a (multi-part) housing 3 and represent a functional unit.
- the (partial) housing 3 of the static coarse classifier 1 forms a (first) classifying room 4, a classifying gas inlet 5, a classifying material inlet 6, a coarse material outlet 7 and a fine material outlet 8.
- a ventilation floor 9 which is oriented obliquely to the vertical and has a large number of ventilation slots (cf. Fig. 3 ).
- the ventilation floor forms a guide level connecting the sight goods inlet 6 with the coarse goods outlet 7.
- Visible material 10 which is introduced into the first classifying room 4 via the classifying material inlet 6, is guided by gravity along this guide level to the coarse material outlet 7 and at the same time flows through the classifying gas flowing through the ventilation slots of the ventilation floor 9.
- the classifying gas entrains sufficiently small and thus light particles of the classifying material 10, the fine material 11.
- the fine material 11 is discharged together with the sight gas flow into the fine material outlet 8 and from there it is fed to the downstream dynamic fine classifier 2.
- the part of the visible material 10 which is not entrained, the coarse material 12 is discharged via the coarse material outlet 7.
- the fine material 11 is fed to the dynamic fine classifier 2 via the fine material outlet 8.
- a fine classifying, larger particles of the fine material 11, the medium-sized material being discharged from the second classifying chamber 13 via a medium-fine material outlet 16, while smaller particles, the very fine material, which in particular is also can be a finished product to be produced, with which the sight gas flow flows out through a fine material outlet 17.
- the static coarse sifter 1 is provided with two bypass channels 18, which are integrated in the (partial) housing 3 of the coarse sifter 1 and are provided for regulatingly passing partial flows of the total flow of the sighting gas entering the sifter via the sighting gas inlet 5 past the first sighting space 4, whereby these partial flows do not take part in the rough view taking place in the first viewing space 4.
- the two bypass channels 18 are arranged on two opposite sides of the first cross-sectional area 4 with fine cross-sections and fine material outlet 8.
- the outer walls of the housing 3 enclose both the bypass channels 18 and the visible space 4 and the fine material outlet 8, while a spatial separation between the bypass channels 18 on the one hand and the visible space 4 and the fine material outlet 8 is realized via two partition walls 19.
- the partitions 19 are extended upstream of the first viewing space 4 (cf. Fig. 4 ) and protrude into the classifying gas inlet 5.
- the partial flows of the classifying gas guided via the bypass channels 18 are separated from the main flow running through the first classifying chamber 4 at a relatively large distance in front of (upstream) the ventilation base 9.
- the branched partial flows are guided within the bypass channels 18 in a plurality of parallel flow channels 21 which are spatially separated by means of partition walls 20.
- Each flow channel 21 has on the input side a control element in the form of a shaft which can be rotated by about 90 ° about a shaft Control flap 22 assigned.
- the volume flow of the partial flows of the sight gas guided through the bypass channels 18 can be controlled between a minimum value, which is essentially zero when the control flaps 22 are completely closed, and a maximum value when the control flaps 22 are fully open.
- the Fig. 6 and 8th show the control flaps 22 in the fully closed position, while in the Fig. 4 a partially open position of the control flaps 22 is shown.
- control flaps 22 are adjusted by means of one actuator 23 per bypass channel, which acts directly on the shaft of one of the control flaps 22, while twisting this one control flap 22 via push-pull rods 24 and levers 25 onto the other control flaps 22 of the respective one Bypass channel 18 is transmitted.
- the partition walls 19 separating the bypass ducts 18 from the first viewing space 4 and the corresponding part of the fine material outlet 8 end at approximately the same height as the partition walls 20 dividing the bypass ducts 18 into the flow ducts 21. Downstream thereof, the housing still forms an outlet space 26 as part the bypass channels 18 (cf. Fig. 5 ). In these outlet spaces 26, the partial flows guided in the individual flow channels 21 of the bypass channels 18 are brought together again and then enter the fine material outlet 8 via an orifice opening 27, which extends only over part of the corresponding side of the fine material outlet 8.
- the two orifices 27 of the two bypass channels 18 are each arranged decentrally and also diametrically to one another with respect to a central longitudinal axis 28 of the fine material outlet 8 (cf. Fig. 9 ; in the Fig. 5 the corresponding diaphragms 30 for the partial spatial separation of the outlet spaces 26 from the fine material outlet 8 are not shown).
- the partial flows entering the fine material outlet 8 from the bypass channels 18 cause a swirl of the then combined total flow of the classifying gas about the central longitudinal axis 28 of the fine material outlet 8.
- the direction of rotation of the swirl corresponds to the direction of rotation of the classifying rotor 14 of the dynamic fine classifier 2.
- the fine material outlet 8 is divided into subspaces by several (here: three) partitions 29, the partitions 29 being oriented transversely and in particular perpendicularly to the ventilation floor 9.
- the intermediate walls 29 serve, on the one hand, to stiffen the housing 3 and, on the other hand, to increase the load-bearing capacity of the main flow of the sight gas, which is reduced as a result of a branching of partial flows conducted via the bypass channels 18, if necessary, by increasing the Froude number.
- the intermediate walls 29 end downstream at approximately the same height as the partition walls 19 and the partition walls 20 and thus upstream of the orifices 27 of the bypass channels 18. As a result, they prevent the partial flows emerging from the bypass channels 18 from being mixed into the main flow of the sighting gas and the formation which occurs in the process of a twist around the central longitudinal axis 28 of the fine material outlet 8 as little as possible.
- Fig. 10 shows a classifier according to a further embodiment.
- the classifier has a static coarse classifier 32 and a dynamic fine classifier 34 connected downstream of it.
- the static coarse sifter 32 is shown in a front view and essentially corresponds to that in FIG Fig. 2 shown static coarse sifter 1 with a ventilation floor 42.
- the static classifier 1 shown in FIG Fig. 10 shown static coarse sifter 32 on a housing 36, which may be tubular or with a rectangular cross section, for example, and serves as a connecting piece between the ventilation base 42 and the fine material outlet.
- Two bypass channels 40 are arranged around the viewing space 38 and within the housing 36, via which partial flows of the total flow entering the static classifier 32 are controllably guided past the ventilation floor 42 and the first viewing space 38.
- the housing 36 extends in an arc towards a dynamic classifier 34 adjoining the static classifier 36, so that the flow flowing through the static classifier 32 is deflected by approximately 180 ° and flows into the dynamic classifier 34.
- the spatial separation of the viewing space 38 and the Fine material outlet of the static classifier 34 and the bypass channels 40 is realized by partition walls 46.
- the partition walls 46 extend along the housing 36 of the static classifier 32.
- the area of the static classifier adjoins the classifying room 38 of the static classifier, in which the material is no longer viewed.
- the partition walls 46 of the bypass channels 40 extend in Fig. 10 over the length of the viewing space 38 and over the length of the housing 36 in which coarse material is separated.
- the dividing walls 46 end in the fine material outlet adjoining the visible space 38 and the bypass flow and the sighted fine material flow are brought together and enter the dynamic classifier 34.
- the fine material leaving the static sifter is fed into the dynamic sifter 34 at the level of the sifting rotor 44 essentially horizontally.
- Fig. 11 shows a classifier according to a further embodiment.
- the in Fig. 11 sifter essentially corresponds to that in Fig. 10 shown classifier with the difference that the partition 48 of the Fig. 11 extends beyond the fine material outlet to the inlet into the dynamic classifier 34.
- the bypass flow and the sighted fine material flow are in the in Fig. 11 Embodiment shown merged downstream of the viewing space 38 and downstream of the fines outlet.
- the partitions 48 end at the downstream end of the fines outlet at the entrance to the dynamic classifier. It is also conceivable that the partition walls 48 extend a little into the gas inlet of the dynamic classifier 34.
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- Combined Means For Separation Of Solids (AREA)
- Separating Particles In Gases By Inertia (AREA)
Description
Die Erfindung betrifft einen Sichter gemäß dem Oberbegriff des Patentanspruchs 1, mit einem Gehäuse, das einen Sichtraum ausbildet, in dem ein oder mehrere Belüftungsböden angeordnet sind und in dem Sichtgut von Sichtgas durchströmt wird, um Feingut von Grobgut zu separieren, wobei ein Sichtgaseinlass und ein Sichtguteinlass in den Sichtraum münden sowie ein Feingutauslass und ein Grobgutauslass aus dem Sichtraum abgehen.The invention relates to a classifier according to the preamble of patent claim 1, with a housing which forms a classifying chamber, in which one or more ventilation floors are arranged and in which classifying gas is flowed through in order to separate fine material from coarse material, a classifying gas inlet and a Visible material inlet opens into the viewing area and a fine goods outlet and a coarse material outlet emerge from the viewing area.
Derartige, auch als statisch arbeitend bezeichnete Sichter dienen der Trennung von Schüttgütern in zwei Fraktionen mit unterschiedlichen Partikelgrößenverteilungen. Die Separierung der Fraktionen erfolgt dabei in dem Sichtraum, in dem das aus dem Sichtguteinlass in Richtung des Grobgutauslasses fallende Sichtgut in Querrichtung von dem Sichtgas durchströmt wird. Dabei werden kleinere Partikel von der Sichtgasströmung mitgerissen und zu dem Feingutauslass transportiert, während größere Partikel über den Grobgutauslass ausgebracht werden.Such classifiers, which are also referred to as statically operating, serve to separate bulk materials into two fractions with different particle size distributions. The fractions are separated in the classifying chamber in which the classifying gas flows through the classifying gas in the transverse direction from the classifying material inlet in the direction of the coarse material outlet. Smaller particles are entrained by the sight gas flow and transported to the fine material outlet, while larger particles are discharged through the coarse material outlet.
Die Belüftungsböden eines statischen Sichters sind mehr oder weniger quer zur Bewegungsrichtung des Sichtguts ausgerichtet, wobei vielfach eine stufenartige Anordnung der Belüftungsböden vorgesehen ist (
Statische Sichter werden vielfach mit dynamischen Sichtern kombiniert, wobei die statischen Sichter dabei regelmäßig als Grobsichter dem als Feinsichter dienenden dynamischen Sichter vorgeschaltet sind. Dynamische Sichter basieren auf einer Trennung von zwei, sich hinsichtlich der Partikelgrößenverteilung unterscheidenden Fraktionen des Sichtguts mittels eines rotierend angetriebenen Sichtkorbs.Static classifiers are often combined with dynamic classifiers, with the static classifiers regularly being upstream as a coarse classifier and serving as a fine classifier. Dynamic classifiers are based on one Separation of two fractions of the material to be classified, which differ in terms of particle size distribution, by means of a rotating driven basket.
Eine Kombination eines statischen Sichters als Grobsichter und eines dynamischen Sichters als Feinsichter in einer Umlaufmahlanlage für Zementklinker ist beispielsweise aus der
Eine Vorrichtung zum Sichten von Schüttgut, bei dem ein statischer Sichter und ein dynamischer Sichter direkt hintereinander geschaltet in ein gemeinsames Gehäuse integriert sind und somit von demselben Sichtgasstrom durchströmt werden, ist aus der
In der
Aus der
Die
Die
Und aus der
Ausgehend von diesem Stand der Technik hat der Erfindung die Aufgabe zugrunde gelegen, eine Möglichkeit anzugeben, die Sichtungswirkung eines statischen Sichters auf möglichst einfache Weise veränderbar vorzusehen.On the basis of this prior art, the object of the invention was to provide a possibility of making the sighting effect of a static classifier changeable in the simplest possible way.
Diese Aufgabe wird durch einen statischen Sichter gemäß dem Patentanspruch 1 gelöst. Vorteilhafte Ausführungsformen davon sind Gegenstand der weiteren Patentansprüche und ergeben sich aus der nachfolgenden Beschreibung der Erfindung.This object is achieved by a static classifier according to claim 1. Advantageous embodiments thereof are the subject of the further claims and result from the following description of the invention.
Der Erfindung liegt zum einen der Gedanke zugrunde, dass der Volumenstrom des durch den statischen Sichter geführten Sichtgases eine einfach beeinflussbare Regelgröße darstellt, deren Veränderung eine relevante Auswirkung auf die Sichtungswirkung des Sichters hat. Insbesondere kann durch eine Veränderung des Volumenstroms des Sichtgases eine Anpassung der Partikelgrößenverteilungen der einerseits als Feingut und andererseits als Grobgut aus dem statischen Sichter abgeführten Materials erfolgen. Dies kann insbesondere in Abhängigkeit von den dem statischen Sichter nachgeschalteten Aggregaten (z.B. eine Mühle oder ein dynamischer Sichter) erfolgen. Auch kann durch eine Anpassung des Volumenstroms eine Veränderung der Trocknungswirkung des (gegebenenfalls erwärmten) Sichtgases erzielt werden.The invention is based on the one hand on the idea that the volume flow of the sight gas guided through the static classifier represents a control variable which can be easily influenced, the change of which has a relevant effect on the Sighting effect of the sifter. In particular, the particle size distributions of the material discharged from the static classifier on the one hand as fine material and on the other hand as coarse material can be adjusted by changing the volume flow of the classifying gas. This can be done, in particular, depending on the aggregates downstream of the static classifier (for example a mill or a dynamic classifier). A change in the drying effect of the (possibly heated) sight gas can also be achieved by adjusting the volume flow.
Dabei könnte grundsätzlich durch eine entsprechende Ansteuerung eines den Sichtgasstrom erzeugenden Gebläses der Volumenstrom des Sichtgases an die vorgesehene Sichtungswirkung eingestellt werden. Nachteilig darin ist jedoch, dass dadurch auch der Volumenstrom des Sichtgases für ein dem statischen Sichter nachgeschaltetes Aggregat, insbesondere einen dynamischen Sichter, verändert wird.In this case, the volume flow of the sight gas could in principle be adjusted to the intended sighting effect by correspondingly controlling a blower generating the sight gas flow. However, it is disadvantageous in this that the volume flow of the classifying gas for an aggregate downstream of the static classifier, in particular a dynamic classifier, is also changed.
Um diesen potentiellen Nachteil zu vermeiden, ist erfindungsgemäß zum einen vorgesehen, den dem statischen Sichter zugeführten Volumenstrom des Sichtgases, bei dem es sich vorzugsweise um Luft handeln kann, dadurch regelbar auszuführen, indem mindestens ein Bypasskanal vorgesehen ist, über den ein Teil des Sichtgasstroms an dem Sichtraum vorbeigeführt wird.In order to avoid this potential disadvantage, the invention provides, on the one hand, for the volume flow of the sight gas supplied to the static classifier, which can preferably be air, to be regulated in such a way that at least one bypass channel is provided, via which part of the sight gas flow is applied is led past the visual space.
Demnach ist ein gattungsgemäßer statischer Sichter, der zumindest ein Gehäuse aufweist, in dem sich der Sichtraum befindet, in dem ein oder mehrere Belüftungsböden angeordnet sind und in dem Sichtgut von Sichtgas durchströmt wird, um das Sichtgut in Feingut und Grobgut zu separieren, wobei (mindestens) ein Sichtgaseinlass und (mindestens) ein Sichtguteinlass in den Sichtraum münden sowie (mindestens) ein Feingutauslass und (mindestens) ein Grobgutauslass aus dem Sichtraum abgehen, durch mindestens einen in das Gehäuse integrierten Bypasskanal zur Umgehung des Sichtraums gekennzeichnet, wobei der Bypasskanal im Sichtgaseinlass abgeht und stromabwärts des Sichtraums mündet.Accordingly, a generic static classifier, which has at least one housing in which the visual space is located, in which one or more ventilation shelves are arranged and in the classifying material of classifying gas, in order to separate the classifying material into fine and coarse material, whereby (at least ) a classifying gas inlet and (at least) one classifying material inlet lead into the classifying room and (at least) one fine material outlet and (at least) one coarse material class exit from the classifying room, characterized by at least one bypass channel integrated in the housing for bypassing the classifying room, the bypass channel going out in the classifying gas inlet and flows downstream of the visual space.
Unter einem Sichtraum wird insbesondere der Bereich des Sichters verstanden, in dem eine Materialsichtung, also eine Abscheidung von Material bestimmter Korngröße erfolgt. Das Material gröberer Korngröße verlässt den Sichtraum über den Grobgutauslass, wobei das Material feinerer Korngröße in den Feingutauslass eintritt. Der Feingutauslass ist dem Sichtraum nachgeschaltet und derart ausgebildet, dass in diesem keine Materialsichtung erfolgt.A viewing space is understood in particular to mean the area of the sifter in which material sifting, that is to say a separation of material, is more specific Grain size is done. The material of coarser grain size leaves the visible space through the coarse material outlet, the material of finer grain size entering the fine material outlet. The fine material outlet is arranged downstream of the visual space and is designed in such a way that no material is viewed in it.
Der Bypasskanal mündet stromabwärts des Sichtraums in den Sichter, wobei der Bypasskanal beispielsweise in den Feingutauslass oder in einen Gaseintritt eines dem ersten Sichter nachgeschalteten zweiten, insbesondere dynamischen, Sichters, mündet.The bypass channel opens into the classifier downstream of the classifying space, the bypass channel opening, for example, into the fine material outlet or into a gas inlet of a second, in particular dynamic, classifier downstream of the first classifier.
Dabei wird unter einem in das Gehäuse integrierten Bypasskanal verstanden, dass zumindest eine (vorzugsweise alle) den Bypasskanal begrenzende, vorzugsweise über die gesamte Länge des Bypasskanals verlaufende Wandfläche Teil des Gehäuses ist und somit neben der Funktion einer Begrenzung des Bypasskanals strukturell (als tragende Wand) oder funktional (z.B. zur Führung eines Mediums) für andere Teile des Sichters genutzt wird.A bypass duct integrated into the housing is understood to mean that at least one (preferably all) wall surface delimiting the bypass duct, preferably extending over the entire length of the bypass duct, is part of the housing and thus, in addition to the function of delimiting the bypass duct, structurally (as a supporting wall) or used functionally (e.g. to guide a medium) for other parts of the classifier.
Durch die Integration des mindestens einen Bypasskanals in das Gehäuse des Sichters können im Vergleich zu einem extern verlaufenden Bypasskanal, der beispielsweise in Form eines Bypassschlauchs ausgebildet sein kann, ein oder mehrere Vorteile generiert werden. Insbesondere kann ein geringerer Platzbedarf, eine bessere Zugänglichkeit von Wartungs- und Inspektionsöffnungen, ein vereinfachtes Verpacken und Transportieren des Sichters und/oder ein verringerter Montageaufwand erzielt werden. Auch Kompensatoren, die bei einem extern verlaufenden Bypasskanal zum Ausgleich von unterschiedlichen Wärmedehnungen erforderlich sein können, können bei einem in das Gehäuse integrierten Bypasskanal entfallen.By integrating the at least one bypass channel into the housing of the classifier, one or more advantages can be generated compared to an externally running bypass channel, which can be designed, for example, in the form of a bypass hose. In particular, a smaller space requirement, better accessibility to maintenance and inspection openings, simplified packaging and transportation of the classifier and / or a reduced assembly effort can be achieved. Compensators, which may be necessary in an external bypass duct to compensate for different thermal expansions, can also be omitted in a bypass duct integrated in the housing.
Für einen erfindungsgemäßen Sichter ist weiterhin vorgesehen, dass dieser einen statischen Grobsichter und einen diesem nachgeschalteten Feinsichter in einem Gehäuse integriert. Demnach ist vorgesehen, dass sich an den Feingutauslass ein zweiter, insbesondere dynamischer, Sichter mit einem zweiten Sichtraum anschließt, wobei ein den zweiten Sichter ausbildendes Gehäuse, das den zweiten Sichtraum umgibt, einen Mittelfeingutauslass und einen Feinstgutauslass ausbildet. Dabei kann insbesondere vorgesehen sein, dass der Feinsichter ein dynamischer Feinsichter ist, der demnach einen in dem zweiten Sichtraum angeordneten, rotierend antreibbaren Sichtrotor, beispielsweise in Form eines konventionellen Sichtkorbs umfasst. Ein solcher Sichter, der einen statischen Grobsichter und einen diesem nachgeschalteten Feinsichter umfasst, kann vorzugsweise in Kombination mit (mindestens) einem für beide (Teil-)Sichter genutzten Gebläse zur Erzeugung der Sichtgasströmung genutzt werden.It is further provided for a classifier according to the invention that it integrates a static coarse classifier and a fine classifier downstream of it in a housing. Accordingly, it is provided that a second, in particular dynamic, classifier with a second classroom is connected to the fine material outlet, a housing forming the second classifier, which forms the second classroom surrounds, forms a medium fine material outlet and a fine material outlet. In particular, it can be provided that the fine classifier is a dynamic fine classifier, which accordingly comprises a rotatingly driven classifying rotor arranged in the second classifying chamber, for example in the form of a conventional classifying basket. Such a sifter, which comprises a static coarse sifter and a fine sifter connected downstream of it, can preferably be used in combination with (at least) one blower used for both (partial) sifters to generate the sifting gas flow.
Die Beeinflussbarkeit des durch den statischen Grobsichter geführten Volumenstroms des Sichtgases durch den Bypasskanal hat insbesondere bei einer solchen Kombination mit einem Feinsichter Vorteile, da auf diese Weise der Volumenstrom durch den statischen Grobsichter weitgehend unabhängig von dem Volumenstrom durch den Feinsichter regelbar ausgeführt werden kann. Insbesondere kann vorgesehen sein, den dem Sichter über den Sichtgaseinlass zugeführten Gesamtvolumenstrom des Sichtgases hinsichtlich des Volumenstrombedarfs des Feinsichters auszulegen und den regelmäßig geringeren Volumenstrombedarf des Grobsichters durch ein Vorbeiführen eines mehr oder weniger großen Teils des Gesamtvolumenstroms an dem (ersten) Sichtraum des Grobsichters anzupassen.The ability to influence the volume flow of the sighting gas through the bypass duct through the static coarse sifter has advantages in particular in the case of such a combination with a fine sifter, since in this way the volume flow through the static coarse sifter can be largely regulated independently of the volume flow through the fine sifter. In particular, provision can be made to design the total volume flow of the sight gas supplied to the classifier via the classifying gas inlet with regard to the volume flow requirement of the fine classifier and to adapt the regularly lower volume flow rate requirement of the classifier by passing a more or less large part of the total volume flow past the (first) viewing area of the classifier.
Um die Einstellbarkeit des über den statischen Grobsichter geführten Volumenstroms des Sichtgases möglichst variabel zu halten, kann vorzugsweise ein Regelelement vorgesehen sein, mittels dessen der freie Strömungsquerschnitt des Bypasskanals (manuell oder automatisiert) veränderbar ist. Das Regelelement kann beispielsweise als mittels eines Stellantriebs verstellbare Regelklappe oder Regelschieber ausgeführt sein.In order to keep the adjustability of the volume flow of the sight gas guided over the static coarse sifter as variable as possible, a control element can preferably be provided, by means of which the free flow cross section of the bypass channel can be changed (manually or automatically). The control element can be designed, for example, as a control flap or control slide adjustable by means of an actuator.
Weiterhin bevorzugt kann vorgesehen sein, dass der Bypasskanal eine Mehrzahl von (räumlich getrennten) Strömungskanälen ausbildet. Dadurch kann eine gleichmäßigere Verteilung der Strömung des über den Bypasskanal geführten Sichtgases und dadurch auch eine gleichmäßigere Einleitung in die Hauptströmung des Sichtgases in dem Feingutauslass erreicht werden.Furthermore, it can preferably be provided that the bypass channel forms a plurality of (spatially separated) flow channels. As a result, a more uniform distribution of the flow of the sight gas guided via the bypass channel and thereby also a more uniform introduction into the main flow of the sight gas in the fine material outlet can be achieved.
Bei einer solchen Ausgestaltung des Bypasskanals kann dann zur Vergleichmäßigung der über die einzelnen Strömungskanäle geführten Teilströmungen des Sichtgases vorgesehen sein, dass für mehrere und insbesondere alle der Strömungskanäle jeweils ein Regelelement vorgesehen ist. Dabei kann auch vorgesehen sein, dass die Regelelemente getrennt verstellbar sind.In such a configuration of the bypass channel, it can then be provided, in order to even out the partial flows of the sight gas that are conducted via the individual flow channels, that a control element is provided for several and in particular all of the flow channels. It can also be provided that the control elements can be adjusted separately.
In einer weiterhin bevorzugten Ausgestaltung des erfindungsgemäßen Sichters kann vorgesehen sein, dass die Strömungskanäle in einem Abstand zu der Mündung des Bypasskanals in den Feingutauslass enden. Dadurch werden die durch die Strömungskanäle geführten Teilströmungen noch vor dem Eintritt in den Feingutauslass und somit noch vor der Vermischung mit der Hauptströmung des Sichtgases wieder vereint. Dies kann sich vorteilhaft hinsichtlich einer möglichst gleichmäßigen Einleitung der über den Bypasskanal geführten Teilströmung des Sichtgases in die Hauptströmung auswirken.In a further preferred embodiment of the classifier according to the invention it can be provided that the flow channels end at a distance from the mouth of the bypass channel into the fine material outlet. As a result, the partial flows through the flow channels are reunited with the main flow of the sight gas before they enter the fine material outlet and thus before they are mixed. This can have an advantageous effect on the most uniform possible introduction of the partial flow of the sight gas into the main flow via the bypass channel.
Besonders vorteilhaft kann ein Vereinen der über die Strömungskanäle geführten Teilströmungen des Sichtgases sein, wenn die über den Bypasskanal geführte Sichtgasströmung über eine im Vergleich zu den Querschnittsabmessungen des Feingutauslasses im Bereich der Mündung des Bypasskanals relativ kleine Mündungsöffnung in den Feingutauslass eingeleitet wird. Dabei kann besonders bevorzugt vorgesehen sein, dass der Bypasskanal dezentral in den Feingutauslass mündet, wodurch mittels der aus dem Bypasskanal in den Feingutauslass eintretenden Sichtgasströmung ein Drall der wieder vermischten Gesamtströmung des Sichtgases erzeugt werden kann, die sich insbesondere positiv auf die Sichtwirkung eines dem statischen Grobsichter nachgeschalteten, dynamischen Feinsichters auswirken kann. Dabei kann vorzugsweise vorgesehen sein, dass die Drehrichtung des Dralls der Sichtgasströmung der Drehrichtung des Sichtrotors des dynamischen Feinsichters entspricht.A combination of the partial flows of the sight gas conducted via the flow channels can be particularly advantageous if the sight gas flow conducted through the bypass channel is introduced into the fine material outlet via a relatively small mouth opening in the area of the mouth of the bypass channel compared to the cross-sectional dimensions of the fine material outlet. It can be particularly preferably provided that the bypass channel opens decentrally into the fine material outlet, whereby a swirl of the re-mixed total flow of the visible gas can be generated by means of the sight gas flow entering the fine material outlet, which in particular has a positive effect on the visual effect of the static coarse sifter downstream, dynamic fine classifier. It can preferably be provided that the direction of rotation of the swirl corresponds to the sight gas flow of the direction of rotation of the sight rotor of the dynamic fine classifier.
Unter "dezentral" wird dabei verstanden, dass die (mittlere) Strömungsrichtung der aus dem Bypasskanal in den Feingutauslass eintretenden Sichtgasströmung (und insbesondere die Mittellängsachse der Mündungsöffnung) die Mittellängsachse der Querschnittsflächen des Feingutauslasses im Bereich der Mündung des Bypasskanals nicht schneidet. Insbesondere kann vorgesehen sein, dass die aus dem Bypasskanal in den Feingutauslass eintretende Sichtgasströmung möglichst weit von der Mittelängsachse und somit möglichst nah an einer den Feingutauslass begrenzenden Wand des Gehäuses eingeleitet wird.“Decentralized” is understood here to mean that the (middle) flow direction of the sight gas flow entering the fine material outlet from the bypass duct (and in particular the central longitudinal axis of the mouth opening) is the central longitudinal axis of the Cross-sectional areas of the fine material outlet in the area of the mouth of the bypass channel do not intersect. In particular, it can be provided that the sight gas flow entering the fine material outlet from the bypass channel is introduced as far as possible from the central longitudinal axis and thus as close as possible to a wall of the housing delimiting the fine material outlet.
Sofern der erfindungsgemäße Sichter mindestens zwei Bypasskanäle aufweist, die vorzugsweise auf sich gegenüberliegenden Seiten des ersten Sichtraums angeordnet sein können, kann für eine erhöhte Drallwirkung der in den Feingutauslass aus den zwei Bypasskanälen eintretenden Sichtgasströmungen vorgesehen sein, dass diese zwei Bypasskanäle nicht nur jeweils dezentral sondern auch zueinander diametral bezüglich einer Mittellängsachse des Feingutauslasses in den Feingutauslass münden.If the classifier according to the invention has at least two bypass channels, which can preferably be arranged on opposite sides of the first classifying room, for an increased swirl effect the sight gas flows entering the fine material outlet from the two bypass channels can be provided that these two bypass channels are not only decentralized but also open diametrically to each other with respect to a central longitudinal axis of the fine material outlet in the fine material outlet.
In einer weiterhin bevorzugten Ausgestaltung des erfindungsgemäßen Sichters kann mindestens eine in dem Feingutauslass angeordnete, quer zu dem oder den Belüftungsböden ausgerichtete Zwischenwand vorgesehen sein. Die Zwischenwand kann zum einen eine Versteifung des Gehäuses bewirken. Zum anderen kann durch die mindestens eine Zwischenwand, die den von dem Feingutauslass ausgebildeten Strömungsraum für die Hauptströmung des Sichtgases in mehrere Teilströmungsräume unterteilt, eine Erhöhung der Tragfähigkeit für die Hauptströmung infolge einer Erhöhung der Froude-Zahl erreicht werden. Dies kann insbesondere bei der erfindungsgemäßen Ausgestaltung eines Sichters relevant sein, bei der ein Teil des Gesamtvolumenstroms des über den Sichtgaseinlass zugeführten Sichtgases bedarfsweise mittels des oder der Bypasskanäle an dem (ersten) Strömungsraum vorbei geführt werden soll.In a further preferred embodiment of the classifier according to the invention, at least one intermediate wall arranged in the fine material outlet and oriented transversely to the ventilation floor or floors can be provided. On the one hand, the intermediate wall can stiffen the housing. On the other hand, an increase in the load-bearing capacity for the main flow as a result of an increase in the Froude number can be achieved by the at least one intermediate wall, which divides the flow space formed by the fine material outlet for the main flow of the sighting gas into a plurality of partial flow spaces. This can be relevant in particular in the design of a classifier according to the invention, in which a part of the total volume flow of the classifying gas supplied via the classifying gas inlet is to be led past the (first) flow space, if necessary, by means of the bypass channel (s).
Damit die Zwischenwand das Einleiten der über den mindestens einen Bypasskanal geführten Sichtgasströmung möglichst nicht behindert, kann vorzugsweise vorgesehen sein, dass der Bypasskanal stromab der Zwischenwand in den Feingutauslass mündet.So that the partition does not hinder the introduction of the sight gas flow conducted through the at least one bypass duct, it can preferably be provided that the bypass duct opens into the fine material outlet downstream of the partition.
Um möglichst zu vermeiden, dass das Abzweigen eines Teils des Volumenstroms des Sichtgases aus der Hauptströmung die Durchströmung des oder der Belüftungsböden negativ beeinflusst, kann weiterhin bevorzugt vorgesehen sein, dass der Bypasskanal in einem (möglichst großen) Abstand vor dem oder den Belüftungsböden aus dem Sichtgaseinlass abgeht. Dies kann konstruktiv einfach dadurch realisiert werden, dass eine den Bypasskanal in den Sichtgaseinlass hinein verlängernde Trennwand vorgesehen wird.In order to avoid, as far as possible, that the branching of a part of the volume flow of the sight gas from the main flow negatively influences the flow through the ventilation plate (s), it can further preferably be provided that the bypass duct is at a (as large as possible) distance in front of the ventilation plate (s) from the sight gas inlet goes off. This can be implemented in a structurally simple manner by providing a partition wall that extends the bypass channel into the sight gas inlet.
Die Erfindung wird nachfolgend anhand eines in den Zeichnungen dargestellten Ausführungsbeispiels näher erläutert. In den Zeichnungen zeigt:
- Fig. 1:
- schematisch einen Sichter in einer Seitenansicht, der einen statischen Grobsichter und einen dynamische Feinsichter kombiniert;
- Fig. 2:
- schematisch den statischen Grobsichter des Sichters in einer Vorderansicht;
- Fig. 3:
- einen Schnitt durch den Grobsichter entlang der Schnittebene III - III in der
Fig. 2 ; - Fig. 4:
- einen Schnitt durch den Grobsichter entlang der Schnittebene IV - IV in der
Fig. 2 ; - Fig. 5:
- den den Sichtraum und den Feingutauslass ausbildenden Teil des statischen Grobsichters in einer perspektivischen Darstellung;
- Fig. 6:
- den Regelelemente zur Regelung der über die Bypasskanäle geführten Teilströmungen des Sichtgases integrierenden Teil des statischen Grobsichters in einer perspektivischen Darstellung;
- Fig. 7:
- eine Seitenansicht des in der
Fig. 6 dargestellten Teils des statischen Grobsichters; - Fig. 8:
- einen Querschnitt durch den in der
Fig. 6 dargestellten Teil des statischen Grobsichters; - Fig. 9:
- schematisch die Erzeugung eines Dralls der Sichtgasströmung in dem Feingutauslass;
- Fig. 10:
- schematisch einen Sichter gemäß einem weiteren Ausführungsbeispiel in einer Vorderansicht, der einen statischen Grobsichter und einen dynamischen Feinsichter kombiniert; und
- Fig. 11:
- schematisch einen Sichter gemäß einem weiteren Ausführungsbeispiel in einer Vorderansicht, der einen statischen Grobsichter und einen dynamischen Feinsichter kombiniert
- Fig. 1:
- schematically a classifier in a side view, which combines a static coarse classifier and a dynamic fine classifier;
- Fig. 2:
- schematically the static coarse classifier of the classifier in a front view;
- Fig. 3:
- a section through the coarse sifter along the section plane III - III in the
Fig. 2 ; - Fig. 4:
- a section through the coarse sifter along the section plane IV - IV in the
Fig. 2 ; - Fig. 5:
- the part of the static coarse sifter forming the viewing space and the fine material outlet in a perspective representation;
- Fig. 6:
- a perspective view of the control elements for controlling the part of the static coarse sifter integrating through the bypass ducts of the classifying gas;
- Fig. 7:
- a side view of the in the
Fig. 6 shown part of the static coarse sifter; - Fig. 8:
- a cross section through in the
Fig. 6 shown part of the static coarse sifter; - Fig. 9:
- schematically the generation of a swirl of the sight gas flow in the fine material outlet;
- Fig. 10:
- schematically a classifier according to a further embodiment in a front view, which combines a static coarse classifier and a dynamic fine classifier; and
- Fig. 11:
- schematically a classifier according to a further embodiment in a front view, which combines a static coarse classifier and a dynamic fine classifier
Der in der
Das (Teil-)Gehäuse 3 des statischen Grobsichters 1 bildet einen (ersten) Sichtraum 4, einen Sichtgaseinlass 5, einen Sichtguteinlass 6, einen Grobgutauslass 7 und einen Feingutauslass 8 aus. In dem ersten Sichtraum 4 ist ein schräg zur Vertikalen ausgerichteter Belüftungsboden 9 vorgesehen, der eine Vielzahl von Belüftungsschlitzen aufweist (vgl.
Über den Feingutauslass 8 wird das Feingut 11 dem dynamischen Feinsichter 2 zugeführt. Durch ein Zusammenwirken eines in einem (zweiten) Sichtraum 13 angeordneten, rotierend angetriebenen Sichtrotors 14 mit Leitschaufeln 15 kommt es zu einer Feinsichtung, wobei größere Partikel des Feinguts 11, das Mittelfeingut, über einen Mittelfeingutauslass 16 aus dem zweiten Sichtraum 13 abgeführt wird, während kleinere Partikel, das Feinstgut, bei dem es sich insbesondere auch um ein herzustellendes Fertiggut handeln kann, mit der Sichtgasströmung über einen Feinstgutauslass 17 abströmt.The
Der statische Grobsichter 1 ist mit zwei Bypasskanälen 18 versehen, die in das (Teil-)Gehäuse 3 des Grobsichters 1 integriert und dazu vorgesehen sind, Teilströmungen der Gesamtströmung des über den Sichtgaseinlass 5 in den Sichter eintretenden Sichtgases an dem ersten Sichtraum 4 regelbar vorbeizuführen, wodurch diese Teilströmungen nicht an der in dem ersten Sichtraum 4 ablaufenden Grobsichtung teilnehmen. Die beiden Bypasskanäle 18 sind auf zwei gegenüberliegenden Seiten des rechteckige Querschnitte aufweisenden ersten Sichtraums 4 und Feingutauslasses 8 angeordnet. Dabei umschließen Außenwände des Gehäuses 3 sowohl die Bypasskanäle 18 als auch den Sichtraum 4 und den Feingutauslass 8, während eine räumliche Trennung zwischen den Bypasskanälen 18 einerseits und dem Sichtraum 4 sowie dem Feingutauslass 8 andererseits über zwei Trennwände 19 realisiert wird.The static coarse sifter 1 is provided with two
Die Trennwände 19 sind dabei stromaufwärts des ersten Sichtraums 4 verlängert ausgeführt (vgl.
Die abgezweigten Teilströmungen werden innerhalb der Bypasskanäle 18 in mehreren parallel verlaufenden, mittels Unterteilungswänden 20 räumlich getrennten Strömungskanälen 21 geführt. Dabei ist jedem Strömungskanal 21 eingangsseitig jeweils ein Regelelement in Form einer um eine Welle um ca. 90° drehbaren Regelklappe 22 zugeordnet. Über die Regelklappen 22 ist der Volumenstrom der über die Bypasskanäle 18 geführten Teilströmungen des Sichtgases zwischen einem bei vollständig geschlossenen Regelklappen 22 vorliegendem Minimalwert, der im wesentlichen Null beträgt, und einem Maximalwert bei vollständig geöffneten Regelklappen 22 regelbar. Die
Ein Verstellen der Regelklappen 22 erfolgt mittels jeweils eines Stellantriebs 23 je Bypasskanal, der direkt auf die Welle jeweils einer der Regelklappen 22 wirkt, während ein Verdrehen dieser einen Regelklappe 22 über Schub-Zug-Stangen 24 und Hebel 25 auf die anderen Regelklappen 22 des jeweiligen Bypasskanals 18 übertragen wird.The control flaps 22 are adjusted by means of one
Die die Bypasskanäle 18 von dem ersten Sichtraum 4 und dem entsprechenden Teil des Feingutauslasses 8 separierenden Trennwände 19 enden in etwa auf derselben Höhe wie die die Bypasskanäle 18 in die Strömungskanäle 21 unterteilenden Unterteilungswände 20. Stromabwärts davon bildet das Gehäuse noch jeweils einen Auslassraum 26 als Teil der Bypasskanäle 18 aus (vgl.
In der
Im Unterschied zu dem voran mit Bezug auf die
- 1.1.
- statischer Grobsichterstatic coarse sifter
- 2.Second
- dynamischer Feinsichterdynamic fine classifier
- 3.Third
- Gehäusecasing
- 4.4th
- erster Sichtraumfirst visual space
- 5.5th
- SichtgaseinlassSight gas inlet
- 6.6th
- SichtguteinlassVisible material inlet
- 7.7th
- GrobgutauslassCoarse material outlet
- 8.8th.
- FeingutauslassFines outlet
- 9.9th
- BelüftungsbodenVentilation floor
- 10.10th
- SichtgutVisible goods
- 11.11th
- FeingutFine goods
- 12.12th
- GrobgutCoarse
- 13.13th
- zweiter Sichtraumsecond visual space
- 14.14th
- SichtrotorClassifying rotor
- 15.15th
- LeitschaufelnGuide vanes
- 16.16th
- MittelfeingutauslassMedium fine outlet
- 17.17th
- FeinstgutauslassFine material outlet
- 18.18th
- BypasskanalBypass channel
- 19.19th
- Trennwandpartition wall
- 20.20th
- UnterteilungswandPartition wall
- 21.21st
- StrömungskanalFlow channel
- 22.22.
- RegelklappeControl flap
- 23.23rd
- Stellantriebactuator
- 24.24th
- Schub-Zug-StangePush-pull rod
- 25.25th
- Hebellever
- 26.26th
- AuslassraumOutlet space
- 27.27th
- MündungsöffnungMouth opening
- 28.28th
- Mittellängsachse des FeingutauslassesCentral longitudinal axis of the fine material outlet
- 29.29.
- ZwischenwandPartition
- 30.30th
- Blendecover
- 31.31st
- statischer Grobsichterstatic coarse sifter
- 32.32nd
- dynamischer Feinsichterdynamic fine classifier
- 36.36th
- Gehäusecasing
- 38.38.
- erster Sichtraumfirst visual space
- 40.40th
- BypasskanalBypass channel
- 42.42nd
- BelüftungsbodenVentilation floor
- 44.44.
- SichtrotorClassifying rotor
- 46.46.
- Trennwandpartition wall
- 48.48.
- Trennwandpartition wall
Claims (15)
- Separator having a housing (3; 36) which configures a separation space (4; 38) in which one or a plurality of ventilation bases (9; 42) are disposed and in which separation stock (10) is perfused by separation gas so as to separate the separation stock into fine stock (11) and coarse stock (12), wherein a separation-gas inlet (5) and a separation-stock inlet (6) open into the separation space (4; 36), and a fine-stock outlet (8) and a coarse-stock outlet (7) lead out of the separation space (4), and wherein at least one bypass duct (18; 40), integrated in the housing (3; 36), for bypassing the separation space (4; 38) is provided, wherein the bypass duct (18; 40) leads out of the separation-gas inlet (5) and opens out downstream of the separation space (4; 38) characterized in that a second separation space (13) of the separator adjoins the fine-stock outlet (8), wherein a housing (3; 36) of the separator which surrounds the second separation space (13) configures a medium-fine stock outlet (16) and a finest-stock outlet (17).
- Separator according to Claim 1, characterized in that the bypass duct (18; 40) opens into the fine-stock outlet (8).
- Separator according to Claim 1, characterized in that the bypass duct (18; 40) opens into an entry of a second separator (2; 32) which has the second separation space (13).
- Separator according to one of the preceding claims, characterized in that a rotatingly drivable separation rotor (14) is disposed in the second separation space (13).
- Separator according to one or a plurality of the preceding claims, characterized in that the bypass duct (18; 40) configures a plurality of flow ducts (21).
- Separator according to one or a plurality of the preceding claims, characterized in that the available flow cross section of the bypass duct (18; 40) is variable by way of a regulator element.
- Separator according to Claims 5 and 6, characterized in that one regulator element is provided for each of a plurality of flow ducts (21).
- Separator according to Claim 7, characterized in that the regulator elements are individually adjustable.
- Separator according to Claim 5 or one of the claims dependent on Claim 5, characterized in that the flow ducts (21) terminate in the fine-stock outlet (8) at a spacing from the port of the bypass duct (18; 40).
- Separator according to Claim 2 or one of the claims dependent on Claim 2, characterized in that the bypass duct (18; 40) opens into the fine-stock outlet (8) in a decentralized manner.
- Separator according to Claim 10, characterized by at least two bypass ducts (18; 40) which in relation to a longitudinal central axis (28) of the fine-stock outlet (8) open into the fine-stock outlet (8) in a decentralized and diametrical manner.
- Separator according to one or a plurality of the preceding claims, characterized by at least one intermediate wall (29) which is disposed in the fine-stock outlet (8) so as to be aligned transversely to the ventilation base(s) (9).
- Separator according to Claim 12, characterized in that the bypass duct (18; 40) opens into the fine-stock outlet (8) downstream of the intermediate wall (29).
- Separator according to one or a plurality of the preceding claims, characterized in that the bypass duct (18; 40) leads out of the separation-gas inlet (5) at a spacing from the ventilation base(s) (9).
- Separator according to one or a plurality of the preceding claims, characterized by a partition wall (19) which extends the bypass duct (18; 40) into the separation-gas inlet (5).
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102014101188 | 2014-01-31 | ||
PCT/EP2015/000180 WO2015113769A1 (en) | 2014-01-31 | 2015-01-30 | Separator with a bypass |
Publications (2)
Publication Number | Publication Date |
---|---|
EP3099426A1 EP3099426A1 (en) | 2016-12-07 |
EP3099426B1 true EP3099426B1 (en) | 2020-03-04 |
Family
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP15703729.2A Active EP3099426B1 (en) | 2014-01-31 | 2015-01-30 | Separator with a bypass |
Country Status (5)
Country | Link |
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US (1) | US10105736B2 (en) |
EP (1) | EP3099426B1 (en) |
CN (1) | CN105939792B (en) |
DK (1) | DK3099426T3 (en) |
WO (1) | WO2015113769A1 (en) |
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Publication number | Priority date | Publication date | Assignee | Title |
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US10597884B2 (en) * | 2017-08-30 | 2020-03-24 | Kelly Slater Wave Company, Llc | Wave pool and wave generator for bi-directional and dynamically-shaped surfing waves |
DE102019123034B3 (en) * | 2019-08-28 | 2020-12-03 | Khd Humboldt Wedag Gmbh | Cyclone with rotating rod basket |
DE102019008657A1 (en) * | 2019-12-13 | 2021-06-17 | Daimler Ag | Particle separator for battery packs and battery pack with particle separator |
Family Cites Families (16)
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---|---|---|---|---|
US2694492A (en) * | 1954-11-16 | Rumpf ettal | ||
US1977479A (en) * | 1933-03-01 | 1934-10-16 | Henry F Hebley | Dust extraction apparatus |
US3398829A (en) * | 1967-02-17 | 1968-08-27 | Du Pont | Apparatus for separating adulterants during pneumatic conveying |
DE2456970C3 (en) | 1974-12-03 | 1981-06-25 | Gebr. Pfeiffer Ag, 6750 Kaiserslautern | Through air sifter |
DE4337215A1 (en) * | 1993-10-30 | 1995-05-04 | Kloeckner Humboldt Deutz Ag | Circulating grinding plant |
CA2311261C (en) * | 1999-06-09 | 2004-02-17 | Mcleod Harvest Inc. | Method and apparatus for harvesting crops |
CA2274288A1 (en) * | 1999-06-09 | 2000-12-09 | Mcleod Harvest Inc. | Method and apparatus for harvesting crops |
DE102004027128A1 (en) | 2004-06-03 | 2005-12-22 | Polysius Ag | Sieve assembly, to sort granular materials into at least three fractions for a mill, has a concentric array of a static and a dynamic sieve around a common axis in a common housing |
DE602005015360D1 (en) * | 2004-11-01 | 2009-08-20 | Comas Spa | METHOD AND DEVICE FOR SORTING A GAS DRIVEN POWER FROM GENERALLY FLAT AND LIGHT ARTICLES |
DE202006014455U1 (en) * | 2006-09-18 | 2006-11-16 | Lhs Clean Air Systems Gmbh | Coarse and fine material separating device for use in separating air current of separator, has outlet that is arranged for purpose of cross flow review of material below upper inlet for separation air on side opposite to inlet of separator |
CN200998711Y (en) * | 2007-01-05 | 2008-01-02 | 上海宝钢冶金技术服务有限公司 | Novel powder selector |
EP2558215B1 (en) * | 2010-04-15 | 2017-03-08 | Allmineral Aufbereitungstechnik GmbH&Co. Kg | Multi-deck air jigging machine |
DE102010054849A1 (en) * | 2010-12-17 | 2012-06-21 | Zeppelin Systems Gmbh | Process and device for separating fine particles from granular bulk materials in a pipeline |
DE102011055762B4 (en) | 2011-11-28 | 2014-08-28 | Maschinenfabrik Köppern GmbH & Co KG | Device for sifting granular material and grinding plant |
CN202460990U (en) * | 2012-02-24 | 2012-10-03 | 贵州成智重工科技有限公司 | Air separation type screening machine |
TWI510279B (en) * | 2014-04-22 | 2015-12-01 | 研能科技股份有限公司 | Powder recycling system |
-
2015
- 2015-01-30 CN CN201580006530.XA patent/CN105939792B/en active Active
- 2015-01-30 EP EP15703729.2A patent/EP3099426B1/en active Active
- 2015-01-30 WO PCT/EP2015/000180 patent/WO2015113769A1/en active Application Filing
- 2015-01-30 DK DK15703729.2T patent/DK3099426T3/en active
- 2015-01-30 US US15/115,748 patent/US10105736B2/en not_active Expired - Fee Related
Non-Patent Citations (1)
Title |
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None * |
Also Published As
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EP3099426A1 (en) | 2016-12-07 |
CN105939792B (en) | 2019-05-31 |
US10105736B2 (en) | 2018-10-23 |
DK3099426T3 (en) | 2020-06-02 |
US20170008034A1 (en) | 2017-01-12 |
CN105939792A (en) | 2016-09-14 |
WO2015113769A1 (en) | 2015-08-06 |
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