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EP1786573A1 - Dispositif pour separer des materiaux de chargement - Google Patents

Dispositif pour separer des materiaux de chargement

Info

Publication number
EP1786573A1
EP1786573A1 EP06791672A EP06791672A EP1786573A1 EP 1786573 A1 EP1786573 A1 EP 1786573A1 EP 06791672 A EP06791672 A EP 06791672A EP 06791672 A EP06791672 A EP 06791672A EP 1786573 A1 EP1786573 A1 EP 1786573A1
Authority
EP
European Patent Office
Prior art keywords
ventilation
width
static
mbar
floor
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
Application number
EP06791672A
Other languages
German (de)
English (en)
Other versions
EP1786573B1 (fr
Inventor
Ludwig KÖNNING
Egbert Burchard
Olaf Hagemeier
Franz-Josef Zurhove
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ThyssenKrupp Industrial Solutions AG
Original Assignee
Polysius AG
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=37309365&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=EP1786573(A1) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Polysius AG filed Critical Polysius AG
Publication of EP1786573A1 publication Critical patent/EP1786573A1/fr
Application granted granted Critical
Publication of EP1786573B1 publication Critical patent/EP1786573B1/fr
Not-in-force legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B07SEPARATING SOLIDS FROM SOLIDS; SORTING
    • B07BSEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
    • B07B9/00Combinations of apparatus for screening or sifting or for separating solids from solids using gas currents; General arrangement of plant, e.g. flow sheets
    • B07B9/02Combinations of similar or different apparatus for separating solids from solids using gas currents
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B07SEPARATING SOLIDS FROM SOLIDS; SORTING
    • B07BSEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
    • B07B4/00Separating solids from solids by subjecting their mixture to gas currents
    • B07B4/08Separating solids from solids by subjecting their mixture to gas currents while the mixtures are supported by sieves, screens, or like mechanical elements

Definitions

  • the invention relates to a device for sifting feedstock with a static sifter having an obliquely oriented to the vertical, traversed by classifying gas ventilation base and a downstream dynamic classifier.
  • a sifter for sifting granular material which has a rod basket classifier and an upstream, shaft-shaped cascade classifier.
  • This cascade classifier has two inclined to the vertical, opposite and between them a caution zone forming Schachtbegrenzungspar, which are permeable to the reformulation.
  • the shaft boundary walls are formed by inclined, louvre-like baffles, which are traversed by view air across.
  • the cascade classifier is operated in circulation operation with a good bed roller mill, the baffles for
  • Deagglomerate i. serve to unlock the scabs formed in the machine bed roll mill.
  • the feed material is fed from above the cascade classifier and falls over the staircase-like baffles down and is thereby deagglomerated and sighted.
  • the fines, along with the classifying air, are fed to the rod cage sifter while the coarse components are led down.
  • the dimensioning of the feed to the separator takes place on the basis of the Gutströme to be handled and provides compact narrow mass flows compared to the classifier.
  • the requirements for a high visual efficiency demand on the one hand the limitation of the feed quantity per classifier width and on the other hand a sufficient number of - from material flow direction - sequentially switched sight levels of the cascade.
  • Another important factor influencing the visual efficiency is the uniformity of the width distribution of the visible material and the classifying air. With wider classifiers, this uniformity is more difficult to realize, which is why the number of vision stages increases with size. With classifiers therefore, the width / height ratio is about 0.15 for small feed quantities and increases to about 0.35 for larger quantities.
  • a sifting device for sifting granular material for large throughput capacities, comprising a static cascade classifier with at least one obliquely arranged viewing zone from the shaft-shaped viewing housing and an angle diverging from the vertical viewing zone and a dynamic rod basket sifter.
  • a special feature is that the sortgasseintrittsgephaseuse the viewing device viewed in plan view has a flow branching on two strands in the manner of a bifurcated tube, wherein in both bifurcated housing branch branches a cantilevered rod basket is arranged.
  • the mirror image opposite arranged front Stabkorb- discharge ends are to the outlet of
  • Fines laden sight gas flow over another housing part merged to form a common trigger housing According to a first variant, a static cascade classifier is arranged in each of the two branch pipe branch branches. In a second variant, a common cascade classifier is provided before the branch.
  • the invention is therefore based on the object to significantly reduce the height of the device for sifting with a static and dynamic sifter and to improve the visual efficiency in viewers with different throughputs. Erf ⁇ ndungshunt this object is achieved by the features of claim 1.
  • the inventive device for sifting feed essentially consists of a static sifter which has a ventilation base which is oriented obliquely to the vertical and through which viewing gas flows
  • Outlet opening for the coarse material a downstream dynamic classifier, which comprises at least one rotor and an outlet opening for the laden with fines sight gas.
  • the ventilation floor has a ratio of width to vertical height of at least 0.45, preferably of at least 0.6.
  • the surface of the ventilation floor is flat and provided with ventilation openings, in particular ventilation slots.
  • the ventilation floor is inclined at an angle between 20 ° and 70 °, preferably between 30 ° and 60 °, to the vertical.
  • Ventilation trays of the devices in a series for different throughputs only in the width and not in the vertical height of each other. This causes in addition to the already much more favorable ratio of width to vertical height and then no increase in height, if the device must be designed with a higher throughput. Further advantages and embodiments of the invention will be explained in more detail below with reference to the description of some exemplary embodiments and the drawing.
  • 1 is a schematic side view of the device for sifting
  • FIG. 2 is a schematic sectional view along the line III-III of Fig. 1,
  • FIG. 3 is a sectional view of the detail III of Fig. 1,
  • FIG. 4 shows a flow chart of a grinding plant with a device according to the invention for sighting
  • Fig. 5 is a side view of a device for sifting with a
  • FIG. 6 is a schematic sectional view along the line VI-VI of Fig. 5,
  • Fig. 7 is a schematic side view of a device for sifting with a
  • FIG. 8 is a schematic, partially sectioned plan view of Fig. 7,
  • Fig. 9 is a schematic view of means for deagglomerating according to a first embodiment
  • FIGS. 1 to 3 are schematic views of deagglomerating means according to a second embodiment.
  • the apparatus 100 for sifting feed material shown in FIGS. 1 to 3 consists essentially of a static sifter 1, which has a ventilation floor Ia oriented obliquely to the vertical, through which viewing gas 2 flows, an inlet opening 3 for discharging the feed material 9 onto the aeration floor Auslassöffhung 4 for the coarse material, a downstream dynamic classifier 5, which comprises at least one rotor 5 a, and at least one Auslassöffhung 6 for the loaded with fines sight gas 2 '.
  • the ventilation floor Ia is inclined at an angle "between 20 ° and 70 °, preferably between 30 ° and 60 °, to the vertical. In the illustrated
  • the surface of the aeration bottom 1 a is flat and provided with ventilation openings Ib, in particular ventilation slots (see Fig. 3).
  • the static classifier 1 and the dynamic classifier 5 are accommodated in a common housing 7, the dynamic classifier being arranged obliquely above the ventilation floor in the side view shown in FIG. 1.
  • the feed material 9 supplied via the inlet opening 3 slips downwards over the ventilation floor 1 a and is thereby traversed transversely by the viewing gas.
  • the fine material of the feed material is carried with the classifying gas 2 to the dynamic classifier, which comprises one or more rotors, in particular rod baskets.
  • the rejected in the region of the rotor medium grain fraction is passed through a disposed within the housing return 8 to 4 Auslassöffhung for the coarse material.
  • the rotor is expediently mounted on both sides and can correspond in its width to the width of the ventilation floor. It would also be conceivable that the width of the rotor is larger or in particular smaller than the width of the
  • Ventilation bottom is formed.
  • a housing transition piece is provided between the static and dynamic classifier, which connects the housing sections of the housing 7 of different widths in the area of the static classifier or the dynamic classifier.
  • the apparatus 100 for sifting with a high-bed roller mill 200 comprises, in addition to the actual classifier, a device 101 for distributing the material to be dispensed across the width of the aeration bottom 1a and means 102 for deagglomerating the material returned from the material bed roller mill 200 to the device for sifting.
  • FIGS. 5 and 6 show a first exemplary embodiment of a device 101 for distributing the feed material over the width of the ventilation floor.
  • This device consists in the illustrated embodiment of baffles which are arranged in the feed chute 7 a of the housing 7.
  • the baffles 101a are designed so that they distribute the feed material 9, which is fed via conveyor 10 in a certain width, to the width b of the ventilation floor Ia.
  • the device 101 is formed by a vibrating groove 101 'a.
  • a bellows breaker 102a according to FIG. 10 is considered, which is expediently arranged below the good-bed roller mill 200.
  • a blower wheel 102'a according to FIG. 9 would also be conceivable, for example.
  • the mass flow of the feed material on the aeration bottom 1 a decreases from top to bottom, since during the residence more and more fines are discharged with the classifying air. This reduces the flow resistance of the feed material in the direction of the outlet opening 4 for the coarse material. So that the classifying air can nevertheless flow uniformly through the feed material, the aeration bottom is designed such that it produces a pressure drop of 2 mbar to 8 mbar, preferably 3 mbar to 4 mbar.
  • the above-described device for sifting is characterized in that the ventilation floors Ia of devices in a series for different throughputs differ only in the width b and not in the vertical height h from each other. This means that the device only increases in width while the overall height remains substantially the same. This, in turn, means that the visual efficiency is substantially the same for devices having different throughputs because, unlike conventional devices, the dwell time, which is essentially determined by the vertical height, remains unchanged.
  • the width of the dynamic rotor is preferably changed linearly with the width of the static ventilation floor.
  • the width of the rotor may differ in principle from the width of the static stage. In particular, the requirements in the final grinding and partial finishing with partial
  • the device according to the invention for the screening of feed material is characterized by a high visual efficiency and, in comparison to the known cascade classifiers, requires a significantly lower overall height, whereby costs are saved.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Combined Means For Separation Of Solids (AREA)
  • Crushing And Grinding (AREA)
  • Disintegrating Or Milling (AREA)
  • Electrical Discharge Machining, Electrochemical Machining, And Combined Machining (AREA)
  • Soil Working Implements (AREA)
  • Apparatus For Radiation Diagnosis (AREA)
  • Glass Compositions (AREA)
  • Sheets, Magazines, And Separation Thereof (AREA)
EP06791672A 2005-09-23 2006-08-25 Dispositif pour séparer des materiaux de chargement Not-in-force EP1786573B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102005045591A DE102005045591A1 (de) 2005-09-23 2005-09-23 Vorrichtung zum Sichten von Aufgabegut
PCT/EP2006/008363 WO2007036276A1 (fr) 2005-09-23 2006-08-25 Dispositif pour separer des materiaux de chargement

Publications (2)

Publication Number Publication Date
EP1786573A1 true EP1786573A1 (fr) 2007-05-23
EP1786573B1 EP1786573B1 (fr) 2010-06-09

Family

ID=37309365

Family Applications (1)

Application Number Title Priority Date Filing Date
EP06791672A Not-in-force EP1786573B1 (fr) 2005-09-23 2006-08-25 Dispositif pour séparer des materiaux de chargement

Country Status (11)

Country Link
US (1) US20080185318A1 (fr)
EP (1) EP1786573B1 (fr)
JP (1) JP5491029B2 (fr)
CN (1) CN101272871B (fr)
AT (1) ATE470514T1 (fr)
BR (1) BRPI0616336A8 (fr)
CA (1) CA2623147C (fr)
DE (2) DE102005045591A1 (fr)
DK (1) DK1786573T3 (fr)
ES (1) ES2344022T3 (fr)
WO (1) WO2007036276A1 (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014056974A1 (fr) 2012-10-10 2014-04-17 Thyssenkrupp Resource Technologies Gmbh Installation de broyage

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102007021545B4 (de) 2007-05-08 2011-07-28 Polysius AG, 59269 Vorrichtung und Verfahren zum Sichten von Aufgabegut und Mahlanlage
DE102011055762B4 (de) 2011-11-28 2014-08-28 Maschinenfabrik Köppern GmbH & Co KG Vorrichtung zum Sichten von körnigem Gut und Mahlanlage
DE102012109645B4 (de) 2012-10-10 2018-11-29 Thyssenkrupp Industrial Solutions Ag Sichter
CN111659619B (zh) * 2020-07-09 2023-11-21 贵州师范大学 一种用于分离苔藓及土壤的分筛装置及其使用方法
CN112076835B (zh) * 2020-09-07 2021-04-06 德州中联大坝水泥有限公司 一种水泥生产制备工艺

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014056974A1 (fr) 2012-10-10 2014-04-17 Thyssenkrupp Resource Technologies Gmbh Installation de broyage

Also Published As

Publication number Publication date
CN101272871B (zh) 2013-03-06
DE502006007156D1 (de) 2010-07-22
BRPI0616336A2 (pt) 2011-06-14
DE102005045591A1 (de) 2007-03-29
JP2009508680A (ja) 2009-03-05
JP5491029B2 (ja) 2014-05-14
CA2623147C (fr) 2015-09-29
CA2623147A1 (fr) 2007-04-05
ATE470514T1 (de) 2010-06-15
BRPI0616336A8 (pt) 2015-04-28
DK1786573T3 (da) 2010-10-04
EP1786573B1 (fr) 2010-06-09
CN101272871A (zh) 2008-09-24
WO2007036276A1 (fr) 2007-04-05
US20080185318A1 (en) 2008-08-07
ES2344022T3 (es) 2010-08-16

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