EP2785472A1 - Device for sifting granular material - Google Patents
Device for sifting granular materialInfo
- Publication number
- EP2785472A1 EP2785472A1 EP12790561.0A EP12790561A EP2785472A1 EP 2785472 A1 EP2785472 A1 EP 2785472A1 EP 12790561 A EP12790561 A EP 12790561A EP 2785472 A1 EP2785472 A1 EP 2785472A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- classifier
- housing
- static
- dynamic
- sifter
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 239000008187 granular material Substances 0.000 title claims abstract description 14
- 230000003068 static effect Effects 0.000 claims abstract description 99
- 239000000463 material Substances 0.000 claims abstract description 75
- 238000009434 installation Methods 0.000 claims abstract description 10
- 238000000227 grinding Methods 0.000 claims description 18
- 238000009826 distribution Methods 0.000 claims description 4
- 230000007704 transition Effects 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 15
- 230000000007 visual effect Effects 0.000 description 11
- 239000004568 cement Substances 0.000 description 7
- 239000000047 product Substances 0.000 description 5
- 238000000926 separation method Methods 0.000 description 4
- 241000237858 Gastropoda Species 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 230000004438 eyesight Effects 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 235000019738 Limestone Nutrition 0.000 description 2
- 238000005054 agglomeration Methods 0.000 description 2
- 230000002776 aggregation Effects 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 239000006028 limestone Substances 0.000 description 2
- 238000003801 milling Methods 0.000 description 2
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 description 2
- 238000012216 screening Methods 0.000 description 2
- 238000004513 sizing Methods 0.000 description 2
- 239000002893 slag Substances 0.000 description 2
- 239000007858 starting material Substances 0.000 description 2
- 241000273930 Brevoortia tyrannus Species 0.000 description 1
- 206010017577 Gait disturbance Diseases 0.000 description 1
- 206010039509 Scab Diseases 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 210000001991 scapula Anatomy 0.000 description 1
- 238000005549 size reduction Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 238000003892 spreading Methods 0.000 description 1
- 230000007480 spreading Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000004382 visual function Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B4/00—Separating solids from solids by subjecting their mixture to gas currents
- B07B4/08—Separating solids from solids by subjecting their mixture to gas currents while the mixtures are supported by sieves, screens, or like mechanical elements
-
- 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
- B07B4/04—Separating solids from solids by subjecting their mixture to gas currents while the mixtures fall in cascades
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C21/00—Disintegrating plant with or without drying of the material
- B02C21/002—Disintegrating plant with or without drying of the material using a combination of a roller mill and a drum mill
- B02C21/005—Disintegrating plant with or without drying of the material using a combination of a roller mill and a drum mill the roller mill having cooperating rollers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C23/00—Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
- B02C23/08—Separating or sorting of material, associated with crushing or disintegrating
- B02C23/10—Separating or sorting of material, associated with crushing or disintegrating with separator arranged in discharge path of crushing or disintegrating zone
- B02C23/12—Separating or sorting of material, associated with crushing or disintegrating with separator arranged in discharge path of crushing or disintegrating zone with return of oversize material to crushing or disintegrating zone
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C23/00—Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
- B02C23/08—Separating or sorting of material, associated with crushing or disintegrating
- B02C23/14—Separating or sorting of material, associated with crushing or disintegrating with more than one separator
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B7/00—Selective separation of solid materials carried by, or dispersed in, gas currents
- B07B7/08—Selective separation of solid materials carried by, or dispersed in, gas currents using centrifugal force
- B07B7/083—Selective separation of solid materials carried by, or dispersed in, gas currents using centrifugal force generated by rotating vanes, discs, drums, or brushes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- 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
Definitions
- the invention relates to an apparatus for sifting granular material into at least three fractions, comprising at least one static sifter forming a first sizing stage and at least one dynamic sifter forming a second sizing stage, the sifter in a sifter housing having at least a first material inlet, at least one sifter inlet and at least one Grobgutaustritt has a plurality of stair-like mutually arranged impact and Leiteinbauten, wherein the dynamic classifier is designed as a rod basket sifter with rotating rod basket and having a second classifier housing with at least one Mittelgutaustritt and a fine material outlet. In the grainy good to be seen, it may, for.
- a generic sighting device of the type described above is known z. B. from DE 42 23 762 B4.
- This classifier has in a housing a rotatably driven rod basket with distributed over the rotor circumference arranged turbo elements and with inlets and outlets for reformluft, reformgut, fines, medium and coarse material.
- the horizontally arranged bar basket is preceded by a shaft-like caution chamber at the same height at the same height, the top of a view of the separate air entry port for the preparegut, the side of the rod basket opposite arranged opening for the classifying air, below a discharge opening for a coarse grain fraction and two opposing, has between it a caution zone forming, for the reformulation permeable Schachtbegren- tion walls.
- WO 03/097241 A1 is also known a generic viewing device, wherein the dynamic classifier - as well as in DE 42 23 762 B4 - is equipped with a rod axis rotating about a horizontal axis.
- the static cascade classifier below the nip of the roller press and above this roller press to arrange the indulgence, which should be designed in particular as a dynamic rod basket sifter.
- a disadvantage is the considerable height in this embodiment.
- the connecting line between the two classifiers increases investment and operating costs.
- An alternative embodiment of a multistage classifier with a compact design is known from US Pat. No. 7,854,406 B2.
- the viewing device consists of a plurality of concentric housings, wherein a rotating about a vertical axis rod basket is provided as a Nachsichttre.
- the precautionary stage is formed by a simple cyclone with the sight and the sighting gas supplied via a common supply line spirally connected to the classifier housing. A deagglomeration of the scapula is limited in the static vision level possible.
- DE 10 2004 027 128 A1 discloses a device for sifting granular material into at least three grain fractions with a static sifter and a dynamic sifter, which are arranged rotationally symmetrically about a common axis in a common housing.
- DE 10 2006 039 775 A1 discloses a classifying device in a special construction with a static cascade classifier and a further classifier as a classifier, wherein the cascade classifier has two packets each spaced above one another and concentrically arranged conical rings.
- DD 253771 A1 describes an air classifier for classifying, in particular, fine-grained bulk materials in at least two fractions, consisting of a cylindrical upper housing part, followed by a semolina cone with semolina discharge at the bottom.
- the rod basket rotates about a vertical axis.
- annular container with a fluidized-bed as dispersing device is provided, which is arranged above the sortgaseintritts- nozzle in the region of the rod basket inside or outside of the classifier housing and communicates with the viewing space via an annular gap and / or an annular channel.
- the known classifiers of the type described have basically proven themselves in practice, but they are capable of further development, in particular with regard to their visual efficiency.
- the invention is therefore an object of the invention to provide a device for sifting granular material in at least three fractions of the type described above, which is characterized not only by a particularly compact design, but in particular by low investment and operating costs and higher visual efficiency.
- a sifting device should enable economical operation of a grinding plant with at least one roller press with high visual efficiency.
- the invention teaches in a generic ago direction for sifting granular material in at least three fractions of a type initially described that
- the static sifter with a z. B. shaft-like and obliquely oriented to the vertical classifier housing is connected directly laterally to the separator housing of the dynamic classifier and passes into this and
- the invention is initially based on the generally known knowledge that it is advantageous to combine a static classifier and a dynamic classifier in the embodiment as Stabkorbsichter together, as on the static classifier a first coarse material fraction can be spied out, so that the dynamic sifter with the relatively sensitive rotating components is not unnecessarily burdened with coarse material.
- a first coarse material fraction can be spied out, so that the dynamic sifter with the relatively sensitive rotating components is not unnecessarily burdened with coarse material.
- the static sifter is connected directly to the side of the dynamic sifter, wherein the static sifter, in terms of process technology, fulfills both the task of the agglomerate agglomeration and a first coarse separation.
- the static sifter and the dynamic sifter are consequently brought together close to each other, so that both sifters work energetically very efficiently and the static sifter can fulfill the task of sludge deagglomeration.
- the classifier of the static classifier opens in tangential or spiral orientation in the classifier of the dynamic classifier.
- the sifter housing of the static sifter merges in the radial direction into the sifter housing of the dynamic sifter.
- embodiments are also included in which the connection of the static separator lies between the tangential orientation and the radial orientation.
- the sifter housing of the static sifter is always compactly connected laterally to the sifter housing of the dynamic sifter so that the static sifter housing merges into the dynamic sifter housing.
- Sifter according to the invention thus has housing areas which can be assigned to both the static classifier and the dynamic classifier as a transition between the static classifier and the dynamic classifier.
- the classifier housing of the dynamic classifier has an upper housing portion in which the rotating rod basket is arranged, and has a lower housing portion, in which z. B. a failure funnel is arranged for the middle goods, wherein the static separator is connected with its housing to the lower housing portion of the dynamic classifier and merges into this lower housing section.
- This lower housing section of the dynamic sifter thus forms the transitional area between static sifter and dynamic sifter.
- the housing of the dynamic classifier may preferably be cylindrical, so that the upper housing portion and / or the lower housing portion may be cylindrical.
- the lower housing section of the dynamic classifier then also has the function of a cyclone, which can influence both the function of the static classifier and the function of the dynamic classifier.
- this cyclone formed by the lower housing section can influence the effect of the static vision level.
- this cyclone as part of the dynamic classifier, since it forms a inflow channel for the vertical admission of the staff basket and since within this housing portion or cyclone also the failure funnel of the dynamic classifier can be arranged.
- the static classifier and the dynamic classifier are spatially and also functionally closely connected.
- the static sifter is preferably connected to the lower housing section of the dynamic sifter. Then the static sifter (in a side view) is usually positioned below the bar basket.
- the static classifier or the static classifier at the same height or at least in some areas at the same height as the rotating rod basket.
- the slide deagglomeration is realized with the help of integrated impact and guide fixtures in the static classifier.
- the baffle and Leiteinbauten can be formed in a conventional manner of mutually inclined baffles or baffles. In a preferred embodiment, these plates or sheets are adjustable in their inclination, z. B. pivotable about a horizontal axis or rotatable.
- the baffles and Leiteinbauten can also be formed by roof-like installations, as z. B. from DE 1 002 600 are known.
- the roof-like installations can optionally be displaced in the horizontal direction.
- the task of puck agglomeration on the one hand and a first coarse material separation on the other hand are always combined.
- the static classifier housing of the dynamic classifier is generally cylindrical or at least partially cylindrical
- the static classifier has a bay-like or box-like housing, which is preferably oriented obliquely to the vertical, so that also arranged inside the baffle and Leiteinbauten are arranged along a slope.
- the shaft-like housing has on the one hand the material inlet or
- the shaft-like housing having a (lower) shaft wall, which at a predetermined angle ⁇ between 10 ° and 80 °, z. B. 40 ° to 60 ° oriented.
- the housing can thus be arranged (in the side view) as a whole obliquely to the vertical.
- the inside of the housing staircase with each other arranged baffles and Leiteinbauten.
- the viewing zone of the first viewing stage is formed, which at a predetermined angle ß between 20 ° and 70 °, z. B. 20 ° to 40 ° oriented relative to the vertical.
- the invention also includes a shaft-like housing, which is not aligned obliquely to the vertical, but parallel to the vertical.
- the preparegaseintritt can z. B. from at least one obliquely above the built-in structures arranged inlet opening are formed.
- the sight gas inlet is formed by one or more openings arranged in the shaft wall.
- These openings can z. B. be closed by flaps, so that can be varied by opening and closing the view gas supply. It is therefore within the scope of the invention that either an (upper) inlet opening of the type described is provided or that openings are provided in the shaft wall.
- a combination of these measures is realized, so that then both at least one obliquely arranged above the internals inlet opening and one or more arranged in the shaft wall openings are provided, said openings optionally z. B. are closed by flaps. It is then possible to work with "variable" air supply and consequently an air flow control. It is expedient if the individual flaps individually, in groups and / or to open and close together, being particularly preferred by
- Flaps means in the context of the invention generally means for opening and closing the openings and in particular for adjusting the air passage rate. Appropriate air flow control offers the possibility of further increasing the visual efficiency.
- the sight gas inlet is formed by a region of the sifter housing which is free of the chute wall. In this embodiment, can be dispensed with the shaft wall, so that then worked with open flow.
- the direction of rotation of the bar basket can be oriented with or against the tangential or spiral connection direction of the static separator housing.
- the dynamic sifter is particularly preferred in the upper part, z. B. in the upper housing section with one or more other material entries see. This is particularly useful when the sifter is integrated into a multi-stage grinding plant, because then the ground good of a second stage can be fed to this sighting over this (second) material inlet. It may be z. B. to the Austragsgut a second crushing device, for. B. a ball mill act.
- the integration of the classifier in a single or multi-stage grinding plant will be explained in more detail below.
- the connection of the plurality of static classifier takes place (in plan view) preferably symmetrical. So it is within the scope of the invention that the plurality of static classifier over the circumference "symmetrical” and therefore arranged equidistantly.
- the offset amounts to 360 n in relation to the circumference, where "n" means the number of static classifiers.
- two static classifiers are preferably connected in plan view at an angle of 180 ° to the dynamic classifier. If three static classifiers are used, these are preferably offset by an angle of about 120 °, and if four static classifiers are used, they are preferably offset by an angle of 90 °, and so on.
- impact installations also in the area of the dynamic classifier, eg. B. within the classifier housing of the dynamic classifier, preferably in the lower housing portion, which can take over the function of a cyclone for the reasons explained.
- the classifier housing of the dynamic classifier is provided with one or more additional air supply lines which perform the function of an air bypass. It is then not only the air supply via the air inlet of the static classifier, but on the dynamic classifier additional air can be supplied. This then leads to the fact that the air supply is reduced in the range of the static classifier, so that in this way an optimized adjustment of the air duct is feasible.
- This additional air supply can, for. B. be realized in the upper housing portion of the classifier housing of the dynamic classifier.
- additional air distribution devices eg. B. perforated plates o. The like., Provide. These can be arranged in the sifter housing of the static classifier in the flow direction in front of the baffles and Leitinstallations. They lead to a better air distribution over the entire height of the static classifier.
- the separator device according to the invention can be used for the sifting of granular materials of various kinds, in particular for the screening of cement, cement raw materials, limestone and similar materials. Alternatively, however, the invention also includes the screening of ores or the like. The natural resources of such raw materials are sometimes largely exploited, so that the extraction moves into hard to reach regions without sufficient water resources. There, the separator according to the invention can be used particularly efficiently.
- the invention also relates to a single-stage (Kreislaufmahlstrom) or multi-stage grinding plant for the crushing of granular material with - at least a first crushing device and
- At least one sorter device of the type described wherein the material emerging from the first crushing material enters the viewing device via the first material inlet and wherein the from the coarse material outlet of the sifting device (or the static separator) exiting coarse material of the first crushing device is supplied, said The middle section or the middle fraction which also leaves the viewing device (or the dynamic classifier) is likewise fed to the first comminution device or alternatively also to a second comminuting device. Consequently, in addition to the first comminuting device, a second comminuting device is also preferably provided, so that an at least two-stage grinding system is then realized.
- the first crushing device may preferably be a good bed roller mill and thus a roller press. In the second crushing device may be, for.
- a multi-level, z. B. two-stage grinding system can be realized, in which in addition to the separator according to the invention, a further, separate separator is provided.
- the middle fraction of the described first classifier according to the invention is in turn subjected to a second size reduction device, e.g. B. supplied to a ball mill.
- the Austragsmaterial this ball mill is then not - as described above - again the first classifier, but the second, separate classifier supplied with the emerging from this second classifier coarse material is again fed to the ball mill, while emerging from the second classifier fines as turn Product can be removed.
- single-stage grinding plants are also encompassed, in which both the coarse material emerging from the sighting device according to the invention and the middle product of a first (single) comminution device, e.g. B. roller press, is fed and wherein the material emerging from this crushing material in turn enters via the material inlet into the viewing device according to the invention.
- a first (single) comminution device e.g. B. roller press
- the first crushing device for. B. roller press
- the roll press is particularly preferably positioned below the classifying device.
- Fig. 1 is a partial vertical section through an inventive
- Fig. 2 is a plan view of the lower part of the article according to
- Fig. 3 is a plan view of the lower part of the article according to
- Fig. 4 shows a modified embodiment of the article according to
- Fig. 5 is a plan view of the lower part of the article according to
- FIG. 6 shows schematically a two-stage grinding plant with a classifying device according to the invention.
- the viewing device 1 shown in FIGS. 1 to 5 is used for sifting granular material, for. As cement, in at least three fractions.
- the device 1 is composed of a static classifier 2 and a dynamic classifier 3, which are combined in a particularly compact manner.
- the static separator 2 forms a first viewing stage
- the dynamic classifier 3 arranged downstream of the static classifier 2 in the direction of the visual medium flow forms a second visual stage.
- the static classifier 2 has a classifier housing 4 with the first material inlet 5, the classifying gas inlet 6 and the coarse material outlet 7. Within the classifier housing 4
- baffles 8, 9 are several, stair-like arranged with each other baffle and Leiteinbauten 8, 9 are arranged.
- these fixtures are designed as baffles 8, 9, which also take over the function of baffles for the static separator.
- Fig. 1 it can be seen that there are two groups of mutually inclined baffle plates 8, 9, wherein these baffles 8, 9 about pivot axes 10 are adjustable, so that the inclination of the baffles 8, 9 is adjustable.
- the second viewing stage is formed by the dynamic classifier 3, which has a classifier housing 11.
- This cylindrical classifier housing 1 1 has an upper (cylindrical) portion 1 1 a and a lower (cylindrical) portion 1 1 b.
- a rotating rod basket 12 is arranged, which surrounds a set of vanes 13. These are stationary vanes, which are arranged at a fixed or adjustable angle of attack to the axis of rotation of the bar basket.
- the rod basket 12 rotates about a vertical axis 14.
- a drive 15 is connected to the rod basket 12.
- Below the bar basket 12 a failure cone 16 is connected within the second classifier housing 1 1, which in turn is connected to the middle goods outlet 17.
- To the upper part 1 1 a of the classifier housing 1 1 of the fine material outlet 18 is connected, via which the gas-fine material mixture is discharged.
- further material inlets 19 are connected to the upper housing part 1 1 a.
- the starting material to be viewed is fed to the sighting device 1 via the first material inlet 5. About this passes the goods to be sighted consequently in the first viewing stage and consequently in the static classifier 2.
- the classifying gas for. B. supplied air. It may be z. B. also act hot drying gases.
- the material to be sighted now falls on the system of baffle and guide plates 8, 9, whereby it is particularly suitable for the Desagglo-
- the slugs and agglomerates produced during milling in a roller press come.
- the material is flowed through by the viewing medium with possible, simultaneous drying.
- the static separator operates as a cross-flow air classifier, so that the coarse material falls through the housing 2 in the lower failure cone 20 and is discharged from there via the coarse material discharge 7.
- This failure cone 20 is structurally connected to the lower part 1 1 b of the classifier housing 1 1 of the dynamic classifier 3.
- the static sifter and the dynamic sifter are interconnected in a very compact manner so that the static sifter 2 merges into the dynamic sifter 3. Because the static separator is connected with its classifier 4 side of the sifter housing 1 1 of the dynamic classifier.
- the classifier housing 4 of the static classifier 2 merges into the lower housing portion 11 b of the classifier housing 1 1, so that the housing portion 11 b of the classifier housing 1 1 is functionally partially on the one hand the static classifier and on the other hand the dynamic classifier can be assigned. It establishes the connection between the static classifier and the dynamic classifier, with the cylindrical lower housing portion 11b also fulfilling the function of a cyclone.
- the selected from the static separator 2 fraction occurs together with the classifying gas in the dynamic classifier 3, namely in the upper portion 1 1 a of the classifier housing 1 1 and there in the area of the staff basket 12. Between this rotating rod basket 12 and the stator blades 13th it comes to the desired Fe Groundung.
- the "coarser” or middle portions reach via the inner failure funnel or failure cone 16 to the failure tube and thus Wegschreibaustritt 17 ("Gr manausfallrohr”).
- This middle fraction is also called “grits”. The fines will be together with
- the gases discharged through the fines and gas outlet 18 from the classifier can be further material directly to the second stage of view perform. It may be z. B. to act, which consists of an additional crushing device, for. B. is fed to a ball mill. This will be discussed in more detail in connection with FIG. 6.
- FIG. 2 and 3 show that the static separator 2 according to the invention with a shaft-like and obliquely arranged to the vertical first withdrawer housing 4 is connected directly to the second classifier housing 1 1 of the dynamic classifier 3, in tangential or spiral embodiment Orientation.
- FIG. 2 shows an embodiment with a spiral connection
- FIG. 3 shows an embodiment with a tangential connection.
- the embodiments according to FIGS. 1 to 3 on the one hand and FIGS. 4 and 5 on the other hand differ in their geometric design, in particular in the area of the static sensor and its guide elements.
- the basic structure and operation are identical.
- the shaft-like first classifier housing which is connected in a tangential or spiral orientation to the second classifier housing, is of particular importance.
- the figures show that this shaft-like first housing 4 or its (lower) shaft wall 21 is oriented at a predetermined angle ⁇ obliquely with respect to the vertical.
- this angle ⁇ is about 40 ° to 60 °, z. B. about 50 °.
- the visual zone of the static classifier formed between the baffle plates 8, 9 which are arranged in the manner of a staircase below one another is oriented obliquely with respect to the vertical at a certain angle.
- this angle ß is about 20 ° to 40 °, z. B. 25 °.
- This overall obliquely oriented housing 4 is according to the invention connected spirally or tangentially to the housing of the dynamic classifier.
- FIGS. 1-10 show an embodiment in which the static classifier, although connected laterally to the dynamic classifier, but is positioned spatially below the rotating rod basket.
- the static classifier is arranged (at least in some areas) at the same height as the rotating rod basket. The same applies to embodiments with multiple static separators.
- the air supply takes place in particular via the illustrated reformgaseinstory 6.
- additional reformgaseinstorye be provided, which are formed in particular by arranged in the shaft wall 21 openings. This is not shown in the figures.
- Such openings may be made by suitable means, e.g. As valves, slides or the like to open and close, in particular by adjustable means a variable adjustment and thus air flow control is possible.
- baffle plates 8, 9 The arrangement of the baffle plates 8, 9 is shown in the figures only by way of example. It is indicated that the articulation points of the baffles 8, 9 need not lie on a common straight line, but may be arranged at a distance from each other. This is indicated in particular in Fig. 4. However, it is alternatively also within the scope of the invention that the articulation points of the baffles or baffles (approximately) are arranged on a straight line or are also toothed and thus formed interlocking. However, they can also - as shown in the figures - be carried out at a distance between the articulation points, wherein this distance is significantly larger in FIG. 4 than in FIG. 1.
- the vertical distance between the individual plates need not be the same, but can vary from plate to plate.
- the plates can also be set at different angles.
- the multistage classifier 1 according to the invention can be particularly preferably integrated into a one-stage or multistage grinding plant, as shown by way of example in FIG.
- a cement grinding plant is shown.
- the multi-level classifier 1 can be seen, which is composed of static classifier 2 and dynamic classifier 3.
- a first crushing device 22 in the embodiment is shown as a roller press, and thus a good bed roller mill 22.
- a second crushing device 23 is shown in the embodiment as a ball mill 23.
- the illustrated two-stage grinding plant works as follows:
- the starting material to be crushed is fed from one or more bunkers 24, z. B. on the transport devices 25, 26, which open via the material inlet 5 in the sighting device 1.
- the coarse material which has been emitted from the coarse material outlet 7 is fed again to the roll press 22. From there it passes via the transport devices 27 and 25, 26 again into the viewing device 1.
- the average material, that is to say the middle fraction, which is oriented from the second visual stage, is fed via the middle product outlet 17 and the transport device 28 to the ball mill 23.
- the grinding plant thus comprises the roller press 22 for the premilling of the material and the ball mill 23 for the post-milling of the material.
- the ball mill 23 is z. B.
- the material emerging from the ball mill 23 is thus supplied via the transport means 29, 32, 33, with which it is brought to the dynamic classifier 3. There it passes through the material inlets 19 again in the second view stage.
- the finest fraction is withdrawn from the sighting device, namely from the dynamic classifier 3 together with the gases through the fine material outlet 18 into the following separation cyclones 34. Here it is separated as a finished product of the gases, which are withdrawn with the fan 35 and partially fed back into the classifier 1 and partially or completely to a dedusting.
- the illustrated two-stage grinding plant can be modified in an alternative embodiment. So z. B. the roller press 22 are placed in contrast to the arrangement shown above the classifying device 1. In this case, the fresh material to be ground is then first fed into the roll press, from which the pre-milled material is guided to the sifter device according to the invention. There, the material is again classified in the manner described in three fractions. This embodiment is not shown. Alternatively, it is also possible to integrate in the two-stage grinding a second, separate viewing device, so that the Austragsgut the ball mill is then not shown in the figures first viewing device, but a not shown, separate second viewing device is supplied. Alternatively, only with a single crushing device, z.
- the visual device according to the invention then form the roller press a "simple", “single-stage” Kreislaufmahlstrom. This is not shown in the figures.
- the multi-stage classifier according to the invention can be used equally for the different types of grinding equipment.
Landscapes
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Mechanical Engineering (AREA)
- Combined Means For Separation Of Solids (AREA)
- Crushing And Grinding (AREA)
Abstract
Description
Claims
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102011055762.8A DE102011055762B4 (en) | 2011-11-28 | 2011-11-28 | Device for sifting granular material and grinding plant |
PCT/EP2012/073513 WO2013079416A1 (en) | 2011-11-28 | 2012-11-23 | Device for sifting granular material |
Publications (3)
Publication Number | Publication Date |
---|---|
EP2785472A1 true EP2785472A1 (en) | 2014-10-08 |
EP2785472B1 EP2785472B1 (en) | 2016-07-20 |
EP2785472B2 EP2785472B2 (en) | 2024-08-07 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP12790561.0A Active EP2785472B2 (en) | 2011-11-28 | 2012-11-23 | Device for classifying grainy products |
Country Status (9)
Country | Link |
---|---|
US (1) | US9636712B2 (en) |
EP (1) | EP2785472B2 (en) |
CN (1) | CN104039466B (en) |
DE (1) | DE102011055762B4 (en) |
DK (1) | DK2785472T4 (en) |
ES (1) | ES2592632T3 (en) |
FI (1) | FI2785472T4 (en) |
IN (1) | IN2014KN01125A (en) |
WO (1) | WO2013079416A1 (en) |
Families Citing this family (25)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
PL232821B1 (en) * | 2013-11-26 | 2019-07-31 | Czech Adam Przed Obrotu Surowcami Wtornymi Hermex | Equipment for cleaning and grain classification of small metallurgical discards and method of cleaning and grain classification of small metallurgical discards |
DE102013020888A1 (en) * | 2013-12-11 | 2015-06-11 | Khd Humboldt Wedag Gmbh | Kreislaufmahlanlage with caution and ball mill |
DK3099426T3 (en) | 2014-01-31 | 2020-06-02 | Thyssenkrupp Ind Solutions Ag | Separator med bypass |
DE102014001384B4 (en) * | 2014-02-01 | 2018-03-29 | Khd Humboldt Wedag Gmbh | Ring-shaped cascade classifier with downstream rod basket sifter |
DE102014108334A1 (en) * | 2014-06-13 | 2015-12-17 | Thyssenkrupp Ag | Grinding plant and process for the comminution of regrind |
CN105363677B (en) * | 2014-08-15 | 2020-05-05 | 中联重科股份有限公司 | Mineral separation device, mineral processing production system, and mineral separation method |
DE102014015549A1 (en) * | 2014-10-22 | 2016-04-28 | Thyssenkrupp Ag | Grinding plant for comminuting regrind and method for comminuting regrind |
DE102014015550A1 (en) | 2014-10-22 | 2016-04-28 | Thyssenkrupp Ag | Sight device for sifting a granular material flow |
US20180243798A1 (en) * | 2015-02-06 | 2018-08-30 | Edw. C. Levy Co. | Closed-Loop Centrifugal Air Classifying System and Method for Utilizing the Same |
DE102015104340A1 (en) * | 2015-03-23 | 2016-09-29 | Maschinenfabrik Gustav Eirich Gmbh & Co. Kg | Molding sand coolers |
DE102015013892B3 (en) * | 2015-10-28 | 2017-02-02 | Khd Humboldt Wedag Gmbh | Pneumatically connected cascade classifier and Kreislaufmahlanlage with pneumatically connected Cascade classifiers |
US10500592B2 (en) * | 2016-03-24 | 2019-12-10 | Schenck Process Llc | Roller mill system with rejects removal system |
DE102016121925A1 (en) * | 2016-11-15 | 2018-05-17 | Neuman & Esser Gmbh Mahl- Und Sichtsysteme | Classifier, mill and method for sifting a gas-solid mixture |
CN107309174A (en) * | 2017-08-25 | 2017-11-03 | 长沙深湘通用机器有限公司 | Sorting unit |
CN107350162A (en) * | 2017-08-25 | 2017-11-17 | 长沙深湘通用机器有限公司 | Multi-product multi-stage classifier |
CN107282447A (en) * | 2017-08-25 | 2017-10-24 | 长沙深湘通用机器有限公司 | Compounding separation machine |
CN107309170A (en) * | 2017-08-25 | 2017-11-03 | 长沙深湘通用机器有限公司 | Many grade-classification machines |
CN108704571B (en) * | 2018-04-28 | 2020-10-02 | 海宁文硕科技咨询有限公司 | Powder raw material feeding mechanism for vanadium-nitrogen alloy production |
DE102018112406A1 (en) * | 2018-05-24 | 2019-11-28 | Netzsch Trockenmahltechnik Gmbh | Process and plant for the production of a starting material for the production of rare earth magnets |
CN109046631B (en) * | 2018-07-23 | 2020-07-28 | 安徽省万佛山农业综合开发有限公司 | Tea processing machine |
DE102018129538B4 (en) * | 2018-11-23 | 2020-10-01 | Khd Humboldt Wedag Gmbh | Pneumatically interconnected multiple sifter |
CN113083459B (en) * | 2021-04-30 | 2023-05-09 | 佛山市硕宸机械设备有限公司 | Grinding and stirring device for producing molten steel heat-insulating covering agent |
CN113477525B (en) * | 2021-07-20 | 2022-06-21 | 天津水泥工业设计研究院有限公司 | Design method of semi-finished product thickness separation powder concentrator with material blocking cone |
CN114700162A (en) * | 2022-03-24 | 2022-07-05 | 张成群 | Integrated sorting and grading machine for powder material processing and grinding system |
CN114871100B (en) * | 2022-05-10 | 2024-01-26 | 合肥工业大学 | Combined aerodynamic three-stage separation equipment and adjusting method thereof |
Family Cites Families (30)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1499721A (en) * | 1919-07-12 | 1924-07-01 | Fraser George Holt | Separator |
DE1002600B (en) | 1955-05-18 | 1957-02-14 | Westfalia Dinnendahl Groeppel | Stream windsifter |
US2956680A (en) * | 1956-01-27 | 1960-10-18 | Babcock & Wilcox Co | Method of and apparatus for separating ash and cleaning shot |
DE3506486A1 (en) | 1985-02-23 | 1986-08-28 | Klöckner-Humboldt-Deutz AG, 5000 Köln | DEVICE FOR CRUSHING AND GRINDING SPROEDEN GROUND MATERIALS, FOR EXAMPLE Cement clinker, ore, coal or the like |
DE3520069A1 (en) | 1985-06-04 | 1986-12-04 | Krupp Polysius Ag, 4720 Beckum | METHOD AND PLANT FOR TWO-STAGE CRUSHING |
DD253771A1 (en) * | 1986-11-21 | 1988-02-03 | Dessau Zementanlagenbau Veb | AIR SEPARATOR |
DE4112018A1 (en) | 1990-06-08 | 1991-12-12 | Kloeckner Humboldt Deutz Ag | SAFE |
JPH0574681A (en) | 1991-09-13 | 1993-03-26 | Nec Corp | Reduction stepper |
JPH0574681U (en) * | 1992-03-11 | 1993-10-12 | 大阪セメント株式会社 | Multi-stage classifier |
DE4223762B4 (en) | 1992-07-18 | 2009-07-23 | Khd Humboldt Wedag Gmbh | Classifying device for sifting granular material and circulation grinding plant with the involvement of such a sifting device |
JPH06106135A (en) * | 1992-09-28 | 1994-04-19 | Ishikawajima Harima Heavy Ind Co Ltd | Multistage air classifier |
DE4337215A1 (en) | 1993-10-30 | 1995-05-04 | Kloeckner Humboldt Deutz Ag | Circulating grinding plant |
DE19751627A1 (en) | 1997-11-21 | 1999-05-27 | Werner Dr Ing Neu | Separator for materials of different densities from heterogeneous mixtures |
DE19944421A1 (en) † | 1999-09-16 | 2001-03-22 | Kloeckner Humboldt Wedag | Classifying device for classifying granular material |
US6405405B1 (en) * | 2000-04-20 | 2002-06-18 | Carter Day International, Inc. | Product cleaner with air flow control |
US6889843B1 (en) * | 2000-10-03 | 2005-05-10 | Polysius Corp. | Apparatus and methods for controlling the separation of particulate material |
DE10119977A1 (en) * | 2001-04-24 | 2002-10-31 | Kloeckner Humboldt Wedag | Production of cement clinker from raw meal comprises adding average grain fraction of an additive from a circulatory grinding device to the raw meal |
DE10142162A1 (en) * | 2001-08-29 | 2003-03-20 | Kloeckner Humboldt Wedag | Sifter for sifting granular material |
DE10221739A1 (en) | 2002-05-16 | 2003-12-04 | Kloeckner Humboldt Wedag | Circular grinding plant with mill and sifter |
US6902126B2 (en) * | 2002-11-04 | 2005-06-07 | Alstom Technology Ltd | Hybrid turbine classifier |
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 |
DE102005045591A1 (en) † | 2005-09-23 | 2007-03-29 | Polysius Ag | Raw material e.g. granular material, separating device for use in grinding plant, has static separator with aeration base through which gas flows, where base is arranged in vertical direction and has specific ratio of breadth to height |
DE102006039775A1 (en) | 2006-08-24 | 2008-02-28 | Khd Humboldt Wedag Gmbh | Sighting device for sifting granular material and Kreislaufmahlanlage with involvement of such a viewing device |
DE102007021545B4 (en) * | 2007-05-08 | 2011-07-28 | Polysius AG, 59269 | Apparatus and method for sifting feed and grinding equipment |
DE102007045373A1 (en) * | 2007-09-22 | 2009-04-02 | Cemag Anlagenbau Gmbh | Method and device for pre- and final grinding of mineral and non-mineral materials |
US7854406B2 (en) | 2008-01-10 | 2010-12-21 | Koppern Equipment, Inc. | Air separator for comminuted materials |
CN201154322Y (en) * | 2008-02-18 | 2008-11-26 | 国投新疆罗布泊钾盐有限责任公司 | Throwing material type crushing vibration screening machine |
DE102008019830B4 (en) * | 2008-04-11 | 2019-01-24 | Khd Humboldt Wedag Gmbh | Circulation meter with external risers |
BRPI0915366B1 (en) * | 2008-07-02 | 2020-10-06 | Bühler AG | PROCESS FOR THE PRODUCTION OF FLOUR AND / OR SEMOL AND EMPLOYMENT OF A MATERIAL BED ROLLER MILL |
CN201807527U (en) * | 2010-07-04 | 2011-04-27 | 李三济 | Spiral rotating sieve |
-
2011
- 2011-11-28 DE DE102011055762.8A patent/DE102011055762B4/en not_active Withdrawn - After Issue
-
2012
- 2012-11-23 US US14/357,153 patent/US9636712B2/en active Active
- 2012-11-23 ES ES12790561.0T patent/ES2592632T3/en active Active
- 2012-11-23 CN CN201280063825.7A patent/CN104039466B/en active Active
- 2012-11-23 IN IN1125KON2014 patent/IN2014KN01125A/en unknown
- 2012-11-23 EP EP12790561.0A patent/EP2785472B2/en active Active
- 2012-11-23 DK DK12790561.0T patent/DK2785472T4/en active
- 2012-11-23 WO PCT/EP2012/073513 patent/WO2013079416A1/en active Application Filing
- 2012-11-23 FI FIEP12790561.0T patent/FI2785472T4/en active
Non-Patent Citations (1)
Title |
---|
See references of WO2013079416A1 * |
Also Published As
Publication number | Publication date |
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ES2592632T3 (en) | 2016-11-30 |
US9636712B2 (en) | 2017-05-02 |
DE102011055762A1 (en) | 2013-05-29 |
WO2013079416A1 (en) | 2013-06-06 |
EP2785472B1 (en) | 2016-07-20 |
DE102011055762B4 (en) | 2014-08-28 |
CN104039466A (en) | 2014-09-10 |
FI2785472T4 (en) | 2024-10-30 |
US20140306044A1 (en) | 2014-10-16 |
EP2785472B2 (en) | 2024-08-07 |
DK2785472T4 (en) | 2024-09-16 |
IN2014KN01125A (en) | 2015-10-16 |
DK2785472T3 (en) | 2016-10-24 |
CN104039466B (en) | 2017-05-24 |
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