EP1561519A1 - Sichteinrichtung für körniges Gut - Google Patents

Sichteinrichtung für körniges Gut Download PDF

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Publication number
EP1561519A1
EP1561519A1 EP04447026A EP04447026A EP1561519A1 EP 1561519 A1 EP1561519 A1 EP 1561519A1 EP 04447026 A EP04447026 A EP 04447026A EP 04447026 A EP04447026 A EP 04447026A EP 1561519 A1 EP1561519 A1 EP 1561519A1
Authority
EP
European Patent Office
Prior art keywords
recovery chamber
cage
chamber
separator according
air
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.)
Withdrawn
Application number
EP04447026A
Other languages
English (en)
French (fr)
Inventor
Xavier Prignon
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.)
Magotteaux International SA
Original Assignee
Magotteaux International SA
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
Application filed by Magotteaux International SA filed Critical Magotteaux International SA
Priority to EP04447026A priority Critical patent/EP1561519A1/de
Priority to PT04802149T priority patent/PT1711281E/pt
Priority to US10/586,236 priority patent/US7780012B2/en
Priority to AT04802149T priority patent/ATE448890T1/de
Priority to DK04802149.7T priority patent/DK1711281T3/da
Priority to CN2004800413776A priority patent/CN1913981B/zh
Priority to AU2004315091A priority patent/AU2004315091B2/en
Priority to PL04802149T priority patent/PL1711281T3/pl
Priority to DE602004024240T priority patent/DE602004024240D1/de
Priority to ES04802149T priority patent/ES2335502T3/es
Priority to BRPI0418068A priority patent/BRPI0418068B1/pt
Priority to RU2006129323/03A priority patent/RU2364448C2/ru
Priority to PCT/BE2004/000173 priority patent/WO2005075115A1/fr
Priority to JP2006551687A priority patent/JP2007520339A/ja
Priority to CA2554725A priority patent/CA2554725C/en
Priority to EP04802149A priority patent/EP1711281B1/de
Publication of EP1561519A1 publication Critical patent/EP1561519A1/de
Priority to ZA200606335A priority patent/ZA200606335B/xx
Withdrawn legal-status Critical Current

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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
    • B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
    • B07B7/00—Selective separation of solid materials carried by, or dispersed in, gas currents
    • B07B7/08—Selective separation of solid materials carried by, or dispersed in, gas currents using centrifugal force
    • B07B7/083—Selective separation of solid materials carried by, or dispersed in, gas currents using centrifugal force generated by rotating vanes, discs, drums, or brushes

Definitions

  • the present invention relates to the separation of granular materials and in particular to the classification of powders or the like with the aid of dynamic air separators.
  • the separation of granular materials and pulvurelents in two granulometric fractions can be do by means of dynamic air separators.
  • the concerned materials are powders with sizes of particles up to 1000 ⁇ m, such as cement, limestone or lime, ore and coal between other.
  • the flows of treated material vary from a few tons to several hundred tons per hour.
  • Dynamic separators have known several major evolutions allowing to classify them in 3 large families.
  • the first generation known usually under the names “turbo”, “heyd” or “Whirlwind” has been improved by the second generation " type wedag ".
  • the 3rd generation is the most effective from the viewpoint of the separation efficiency.
  • the operating principle of the separators (O'Sepa, Sturtevant SD, 7) is described in the documents USP 4,551,241 and EP 0023320.
  • US 4,551,241 discloses a particle separator with a lateral cyclone in which particles are returned to be cycloned. The surplus being returned to the rotating cage of separator. The entire installation turns out relatively bulky and quite complex design.
  • EP 0023320 also presents a device for the classification of granular materials with a side outlet for air loaded in fines particles. This installation requires the use of additional filters and / or cyclones for separation fine materials.
  • the present invention aims to disclose a dynamic air separator to avoid the use of external filters or cyclones, the recovery of fines occurring in the body of separator itself.
  • the present invention also relates to a granulometric separation process using the separator of the invention.
  • said recovery chamber 2 may have baffles fixed and / or mobile (4.7) to change the air speed and / or change the direction of it.
  • said recovery chamber 2 of the fine materials is cylindrical or frustoconical, the cone can be opened upwards or downwards.
  • said chamber of recovery 2 of the fine materials has a length that corresponds to 2 to 6 times the length of the rotating cage 1 to have a necessary cyclone capacity and sufficient.
  • said recovery chamber 2 of the fine materials and said cage rotating 1 have the same vertical axis as the chamber recovery 2 located below and in the extension of said cage 1.
  • the deflectors 4 which are positioned in the outgoing part of the rotating cage 1 and / or in the recovery chamber 2, are trained by the means of rotation of the cage 1, or by a separate device
  • the deflectors 4 which are positioned in the outgoing part of the rotating cage 1 are attached to said cage 1 itself.
  • the invention further specifies that the conduit air outlet 3 crosses the bottom outlet of the recovery chamber 2, said duct having a diameter between 30 and 95% of the diameter of the bottom of the chamber recovery 2 fine materials.
  • a plurality of openings and / or slots is disposed in the bottom of the chamber of recovery 2.
  • conduits 8 leading to a means of transporting the material.
  • ducts 8 leading to a circular hovercraft transporting the material to another means of transport.
  • the separator of the invention is characterized also by the presence above the bottom of the room 2, outside the pipe of evacuations of the air 3, of one or more deflectors 7 tapered, cylindrical or radial (inclined or straight), so to minimize the turbulence around the bottom of the room and avoid the recovery of the material by the air.
  • the invention also shows the presence of a plurality of openings in the part lower envelope 5 of the recovery chamber 2, these openings ending in harvesting ducts fine material that can be properly placed (not shown)
  • the invention discloses the use of device described in claim 1 for the separation and classification of particles of matter mineral such as cement particles, clinker, lime and coal.
  • FIG. 1 shows the diagram of a 3rd generation separator according to prior art.
  • FIG. 2 shows the schematic diagram of the separator of the invention.
  • the heart of the separator consists of a squirrel cage 1 rotating around a vertical axis.
  • This cage is consists of spaced plates or bars and is surrounded 14 vents to guide the air before entering by the inlet volute 6 in the cage 1. Les ventelles 14 can also participate in the management of the airflow.
  • the material to be separated ends up in the zone of selection delimited by the outside of cage 1 and the deflectors 4.
  • the maximum size of incoming particles in the cage with the air will be determined by the speed of rotation of cage 1 and the amount of air with which the separator will be fed.
  • the larger particles remain at the outside of the cage and are recovered in the room 17. These large particles come out of the separator by gravity 10.
  • the air charged with fine particles 15 leaves of the cage either from above or sideways and leaves the separator by a pipe.
  • the recovery of the material fine is then done by means of cyclone (s) or filter (s) outside (s) to the separator body.
  • the air enters the cage 1 with a tangential speed of the same order of magnitude as the circumferential speed of the cage.
  • the tangential component of the velocity increases naturally with the penetration of the air inside the cage 1 (vortex effect).
  • the principle of the invention is schematized in Figure 2. This one consists in using the vortex already created to cyclone the material to be treated 13 in a recovery chamber 2 adjacent and coaxial to the cage 1, the dusted air 12 leaving this room recovery 2 by an exhaust duct 3 of which the entrance is located inside the room of recovery 2. The dusted air 12 is then sucked to one or more fans that return the air in part or in total towards the air inlet volute 6 of the separator.
  • the vortex created by the rotating cage 1 can either remain free or be accelerated by deflectors fixed or movable 4 before entering that chamber of recovery 2. These deflectors 4 can also be located in the recovery chamber 2 itself.
  • the fine material 11 is centrifuged in this recovery chamber 2 and will focus in the outer part of the room where it will be harvested means of openings in the walls (cylindrical envelope and / or bottom) of the recovery chamber 2.
  • Material recovery efficiency fine 11 depends essentially on the particle size and their absolute density. With equal matter the factors important are the intensity of the vortex, that is the tangential velocity of air throughout the chamber of recovery 2, the diameter of the recovery chamber 2 and the residence time of the particles in said chamber.
  • the important factors will be the diameter of the recovery chamber 2, the length of it and the tangential velocity of the air. More tangential component of the air is important and the longer the room, the better the performance of recovery.
  • the invention therefore consists of a separator to cage, equipped with a recovery chamber of fine materials 2 which is installed coaxially in the extension of the rotating cage 1.
  • This fine recovery chamber is cylindrical or conical (frustoconical), the angle of the generator of the cone with the axis of revolution of the cone being preferably less than 30 °, the inlet diameter of the recovery chamber 2 of fine materials is the same order of magnitude than the diameter of the cage 1 and a length corresponding to 2 to 6 times the length of the cage 1.
  • cage 1 and / or in the recovery chamber 2 can be installed fixed or movable deflectors 4 for influencing the direction of the air nets.
  • the possible rotation of these deflectors 4 can be made by fixing them on the cage 1 or then be set in motion by a independent drive of the cage 1. They can also be trained by the same means as cage 1 without being fixed on said cage 1.
  • the exhaust duct 3 of the air discharged from matter 12 will be on its first part concentric to the recovery chamber and will preferably have a diameter between 0.3 and 0.95 times the diameter of the bottom of the recovery chamber 2 in the plane of the surface input of said conduit.
  • Outlet baffles 7 can be arranged to control the direction air inlet at the entrance of the pipe.
  • the recovery of the centrifuged material is by the application of openings on the output background and / or on the lower half of the envelope 5 of the chamber of recovery 2. Sheaths or ducts of material 8 are arranged in front of these openings to collect and guide the material towards conventional means of transport.
  • the invention avoids the use of filters or cyclones external to the machine facilitating by consequently its implantation.
  • An added benefit lies in the fact that the separation set is no longer compact, which decreases the engineering work for implementation, reduces installation costs and decreases the pressure drops in the separation circuit.

Landscapes

  • Cyclones (AREA)
  • Combined Means For Separation Of Solids (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Centrifugal Separators (AREA)
  • Polysaccharides And Polysaccharide Derivatives (AREA)
  • Glass Compositions (AREA)
  • Disintegrating Or Milling (AREA)
  • Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
EP04447026A 2004-02-04 2004-02-04 Sichteinrichtung für körniges Gut Withdrawn EP1561519A1 (de)

Priority Applications (17)

Application Number Priority Date Filing Date Title
EP04447026A EP1561519A1 (de) 2004-02-04 2004-02-04 Sichteinrichtung für körniges Gut
ES04802149T ES2335502T3 (es) 2004-02-04 2004-12-08 Separador de material granuloso.
BRPI0418068A BRPI0418068B1 (pt) 2004-02-04 2004-12-08 classificador a ar dinâmico e método de separação
AT04802149T ATE448890T1 (de) 2004-02-04 2004-12-08 Trennvorrichtung für körniges material
DK04802149.7T DK1711281T3 (da) 2004-02-04 2004-12-08 Separator til granuleret materiale
CN2004800413776A CN1913981B (zh) 2004-02-04 2004-12-08 颗粒状物质的气动分离器和由该气动分离器进行颗粒分离的方法
AU2004315091A AU2004315091B2 (en) 2004-02-04 2004-12-08 Separator for granular material
PL04802149T PL1711281T3 (pl) 2004-02-04 2004-12-08 Separator substancji ziarnistych
DE602004024240T DE602004024240D1 (de) 2004-02-04 2004-12-08 Trennvorrichtung für körniges material
PT04802149T PT1711281E (pt) 2004-02-04 2004-12-08 Separador de matéria granulosa
US10/586,236 US7780012B2 (en) 2004-02-04 2004-12-08 Classifier for granular material
RU2006129323/03A RU2364448C2 (ru) 2004-02-04 2004-12-08 Сепаратор сыпучего материала
PCT/BE2004/000173 WO2005075115A1 (fr) 2004-02-04 2004-12-08 Separateur de matiere granuleuse
JP2006551687A JP2007520339A (ja) 2004-02-04 2004-12-08 粒状材料のための分級機
CA2554725A CA2554725C (en) 2004-02-04 2004-12-08 Separator for granular material
EP04802149A EP1711281B1 (de) 2004-02-04 2004-12-08 Trennvorrichtung für körniges material
ZA200606335A ZA200606335B (en) 2004-02-04 2006-07-31 Separator for granular material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP04447026A EP1561519A1 (de) 2004-02-04 2004-02-04 Sichteinrichtung für körniges Gut

Publications (1)

Publication Number Publication Date
EP1561519A1 true EP1561519A1 (de) 2005-08-10

Family

ID=34673774

Family Applications (2)

Application Number Title Priority Date Filing Date
EP04447026A Withdrawn EP1561519A1 (de) 2004-02-04 2004-02-04 Sichteinrichtung für körniges Gut
EP04802149A Active EP1711281B1 (de) 2004-02-04 2004-12-08 Trennvorrichtung für körniges material

Family Applications After (1)

Application Number Title Priority Date Filing Date
EP04802149A Active EP1711281B1 (de) 2004-02-04 2004-12-08 Trennvorrichtung für körniges material

Country Status (16)

Country Link
US (1) US7780012B2 (de)
EP (2) EP1561519A1 (de)
JP (1) JP2007520339A (de)
CN (1) CN1913981B (de)
AT (1) ATE448890T1 (de)
AU (1) AU2004315091B2 (de)
BR (1) BRPI0418068B1 (de)
CA (1) CA2554725C (de)
DE (1) DE602004024240D1 (de)
DK (1) DK1711281T3 (de)
ES (1) ES2335502T3 (de)
PL (1) PL1711281T3 (de)
PT (1) PT1711281E (de)
RU (1) RU2364448C2 (de)
WO (1) WO2005075115A1 (de)
ZA (1) ZA200606335B (de)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111021371A (zh) * 2019-12-31 2020-04-17 广东省第一建筑工程有限公司 一种溶洞基坑支护施工方法
FR3128386A1 (fr) 2021-10-27 2023-04-28 Cool Clean Researches And Technologies Séparateur granulométrique

Families Citing this family (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA2400258C (en) 2002-09-19 2005-01-11 Suncor Energy Inc. Bituminous froth inclined plate separator and hydrocarbon cyclone treatment process
US7736501B2 (en) 2002-09-19 2010-06-15 Suncor Energy Inc. System and process for concentrating hydrocarbons in a bitumen feed
CA2476194C (en) 2004-07-30 2010-06-22 Suncor Energy Inc. Sizing roller screen ore processing apparatus
CA2567644C (en) 2005-11-09 2014-01-14 Suncor Energy Inc. Mobile oil sands mining system
US8393561B2 (en) 2005-11-09 2013-03-12 Suncor Energy Inc. Method and apparatus for creating a slurry
CA2526336C (en) 2005-11-09 2013-09-17 Suncor Energy Inc. Method and apparatus for oil sands ore mining
US8168071B2 (en) 2005-11-09 2012-05-01 Suncor Energy Inc. Process and apparatus for treating a heavy hydrocarbon feedstock
JP4786410B2 (ja) * 2006-05-18 2011-10-05 前澤工業株式会社 沈砂分離設備
CA2640514A1 (en) 2008-09-18 2010-03-18 Kyle Alan Bruggencate Method and apparatus for processing an ore feed
CA2689021C (en) 2009-12-23 2015-03-03 Thomas Charles Hann Apparatus and method for regulating flow through a pumpbox
BE1020252A3 (fr) * 2011-09-14 2013-07-02 Magotteaux Int Separateur de matieres granuleuses.
CN103041936B (zh) * 2011-10-15 2015-04-08 高苏茂 涡旋加速除尘器
CN102489445A (zh) * 2011-12-26 2012-06-13 崔建 小粒径树脂与水的分离槽
GB2528445B (en) 2014-07-21 2018-06-20 Edwards Ltd Separator apparatus
DE102015104340A1 (de) 2015-03-23 2016-09-29 Maschinenfabrik Gustav Eirich Gmbh & Co. Kg Formsandkühler
US10287171B2 (en) * 2016-05-05 2019-05-14 Rec Silicon Inc Tumbling device for the separation of granular polysilicon and polysilicon powder
CN105944493B (zh) * 2016-07-13 2018-04-03 辽宁天泽产业集团大庆天泽有限公司 一种具有多层过滤网的灰尘集中过滤器
CN109865215B (zh) * 2019-01-31 2021-04-13 中煤科工集团重庆研究院有限公司 一种呼吸性粉尘分离装置
DE102019123034B3 (de) * 2019-08-28 2020-12-03 Khd Humboldt Wedag Gmbh Zyklon mit rotierendem Stabkorb

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DE1407270A1 (de) * 1956-12-04 1969-01-16 Steinmueller Gmbh L & C Sichteinrichtung hinter Mahlanlagen
US4551241A (en) * 1984-02-08 1985-11-05 Sturtevant, Inc. Particle classifier
US5232096A (en) * 1990-11-08 1993-08-03 Christian Pfeiffer Maschinenfabrik Gmbh & Co. Kg Material dispersion apparatus

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Publication number Priority date Publication date Assignee Title
DE1407270A1 (de) * 1956-12-04 1969-01-16 Steinmueller Gmbh L & C Sichteinrichtung hinter Mahlanlagen
US4551241A (en) * 1984-02-08 1985-11-05 Sturtevant, Inc. Particle classifier
US5232096A (en) * 1990-11-08 1993-08-03 Christian Pfeiffer Maschinenfabrik Gmbh & Co. Kg Material dispersion apparatus

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111021371A (zh) * 2019-12-31 2020-04-17 广东省第一建筑工程有限公司 一种溶洞基坑支护施工方法
FR3128386A1 (fr) 2021-10-27 2023-04-28 Cool Clean Researches And Technologies Séparateur granulométrique

Also Published As

Publication number Publication date
ATE448890T1 (de) 2009-12-15
DE602004024240D1 (de) 2009-12-31
ZA200606335B (en) 2007-12-27
CA2554725A1 (en) 2005-08-18
DK1711281T3 (da) 2010-03-08
EP1711281B1 (de) 2009-11-18
EP1711281A1 (de) 2006-10-18
US20070163925A1 (en) 2007-07-19
CN1913981B (zh) 2010-09-29
RU2006129323A (ru) 2008-03-10
WO2005075115A1 (fr) 2005-08-18
PL1711281T3 (pl) 2010-04-30
AU2004315091B2 (en) 2010-08-12
CA2554725C (en) 2012-04-03
ES2335502T3 (es) 2010-03-29
JP2007520339A (ja) 2007-07-26
RU2364448C2 (ru) 2009-08-20
PT1711281E (pt) 2010-02-05
AU2004315091A1 (en) 2005-08-18
CN1913981A (zh) 2007-02-14
BRPI0418068B1 (pt) 2016-08-23
BRPI0418068A (pt) 2007-04-17
US7780012B2 (en) 2010-08-24

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