EP3461565A1 - Séparateur - Google Patents

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Publication number
EP3461565A1
EP3461565A1 EP18203588.1A EP18203588A EP3461565A1 EP 3461565 A1 EP3461565 A1 EP 3461565A1 EP 18203588 A EP18203588 A EP 18203588A EP 3461565 A1 EP3461565 A1 EP 3461565A1
Authority
EP
European Patent Office
Prior art keywords
air
dispersing
baffles
classifier
guide
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
EP18203588.1A
Other languages
German (de)
English (en)
Other versions
EP3461565B1 (fr
Inventor
Joachim Galk
Thomas Mingers
Marc Giersemehl
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.)
Neuman & Esser Process Technology GmbH
Original Assignee
Neumann & Esser Process Technology GmbH
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
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Publication of EP3461565A1 publication Critical patent/EP3461565A1/fr
Application granted granted Critical
Publication of EP3461565B1 publication Critical patent/EP3461565B1/fr
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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
    • B07B11/00—Arrangement of accessories in apparatus for separating solids from solids using gas currents
    • B07B11/06—Feeding or discharging arrangements
    • 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
    • B07B4/025—Separating solids from solids by subjecting their mixture to gas currents while the mixtures fall the material being slingered or fled out horizontally before falling, e.g. by dispersing 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
    • 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 invention relates to a separator according to the features of the preamble of claim 1.
  • the DE 38 23 380 C2 discloses such a separator with a spreading plate on which the material to be treated is applied centrally. Over the circumference of the spreading plate impact elements on the upper side and radially outwardly projecting impact elements are fixed rigidly or freely oscillating below the outer edge.
  • the spreading plate is driven independently of the rod basket. On the spreading plate in the center of a task cone is arranged, which has the task of redirecting the falling feed on the spreading plate. Due to the centrifugal forces, the feed material slips to the edge of the spreading plate, wherein the feed material at the same time a component of movement in the direction of rotation of the spreading plate is mediated. At the edge of the spreading plate, the feed material hits the striking elements arranged on the spreading plate, so that the aggregates are comminuted at this point.
  • the particles of the feed material meet on outwardly projecting further impact elements of the spreading plate.
  • baffles which are arranged on the inside of the classifier housing above the viewing zone between the rod basket and the vane ring, the estate should be concentrated in the beat circle of the impact elements of the staff basket are passed. Despite various measures, deagglomeration is unsatisfactory.
  • the DE 43 02 857 A1 discloses a cleaning apparatus for cleaning a corn stack comprising a spreader to which is attached both a hood and a truncated cone which in turn carries a cone. Impact elements are not provided.
  • the WO 2014/124899 A1 describes a sifter which has in the visual zone between the air guide system and the rotor cage internals, which are intended to cause the agglomerated feed particles are at least partially disagglomerated. This should make a more efficient sighting possible.
  • the internals are arranged such that they extend parallel to the axis of rotation of the rotor cage or form an angle with the rotor axis.
  • the internals which can also be formed by end portions of the guide vanes of the air duct system, form bottlenecks or constrictions in the circumferential direction of the viewing zone.
  • the DE 199 61 837 A1 also installations in the form of protruding into the viewing zone guide flaps are to be taken, which extend parallel to the axis of the dynamic rotor part.
  • the EP 1 529 568 B1 discloses a cyclone separator in which the flow cross-section is constricted in the flow direction of the product before the deposition area at at least one point.
  • diaphragms are used, such as conical rings, which can be installed in several places in the viewing zone.
  • the separator according to claim 1 is characterized in that the task cone is arranged at a distance from the dispersing plate on the housing.
  • the particles of the feed material and in particular the agglomerates of the feed material have only one vertical and one radial movement component.
  • the agglomerates slide off the task cone, the agglomerates are caught and smashed by the dispersing blades of the dispersing disk rotating beneath the task cone.
  • the dispersing blades are arranged distributed on the upper side of the dispersing disk over the circumference of the dispersing disk.
  • dispersing blades Preferably, four to twenty dispersing blades are provided.
  • the impact of the dispersing blades is significantly greater than in the prior art, because the agglomerates on impact with the dispersing blades still have no component of motion in the direction of rotation of the dispersing.
  • the selectivity of the classifier is significantly improved, because not only a significantly larger amount of agglomerates is deagglomerated, but the agglomerates are almost completely decomposed into their original individual particles.
  • the task cone has an opening angle ⁇ with 45 ° ⁇ ⁇ ⁇ 90 °.
  • This is a pointed cone, which has the advantage that the slope of the conical surface is large and thereby the particles of the feed material in their vertical movement are slowed down only slightly before they hit the dispersing blades.
  • the task cone has a radius R 1 at its cone edge, for which 0.5 x R 2 ⁇ R 1 ⁇ R 2 , where R 2 denotes the radius of the dispersing plate. If this relationship is maintained, it is ensured that the cone edge of the task cone extends as far as possible to the edge of the dispersing plate and thus strike the particles of the feed material on a region of the dispersing disk and the dispersing blades which has a correspondingly high web speed v.
  • the impulse p mxv acting on the agglomerates is greater, the greater the orbital velocity v. It is therefore advantageous to choose the radius R 2 of the dispersing plate as large as possible, because then also the radius R 1 of the cone edge within the range 0.5 x R 2 to R 2 can be made large.
  • the web speed v at the radially outer end of the dispersing blades is preferably in the range from 40 m / s to 150 m / s, in particular in the range from 80 m / s to 150 m / s.
  • R 1 must not be too large, so that the falling agglomerates from the task cone do not shoot over the edge of the dispersing plate due to their radial velocity. It is therefore preferred to choose R 1 ⁇ 0.9 ⁇ R 2 , in particular R 1 ⁇ 0.8 ⁇ R 2 .
  • the radius R 3 of the inner circumference of the Dispergierschaufeln R 3 ⁇ R. 1 The inner circumference of the dispersing blades designates the circle on which the inner surfaces of the dispersing blades point radially to the center of the dispersing disk.
  • the distance A 1 between the cone edge of the dispensing cone and the dispersing blades of the dispersing disk is preferably 0 ⁇ A 1 ⁇ 30 mm and is particularly preferably 5 mm to 30 mm, in particular 5 mm to 25 mm.
  • the advantage of a small distance A 1 is that the agglomerates of the feed material immediately after leaving the task cone are detected by the dispersing blades and smashed.
  • each dispersing blade has a dispersing surface, which is arranged perpendicular to the direction of rotation of the dispersing plate. This has the advantage that a maximum force on the impinging agglomerates of the feed material is ensured.
  • the dispersing blades are upstanding at the top of the dispersing disk and extending in radial directions.
  • a baffle ring is provided on the housing, which has distributed over the circumference, in the direction of the dispersing plate projecting baffle elements.
  • the baffle ring is preferably arranged stationary on the housing.
  • 24 or more than 24 baffles are provided.
  • the particles of the feed material which are thrown by the impact ring due to the centrifugal forces to the outside, not only hit against the baffle ring, but due to their component of motion in the direction of rotation of the turntable and against the baffles.
  • the advantage of the baffle ring with the baffle elements is that agglomerates, which may not yet have been completely broken down into the individual particles by the dispersing blades of the dispersing plate, can be effectively comminuted in this second stage of the dispersion. The deagglomeration is thereby further improved.
  • the distance A 2 between the baffle elements and the dispersing plate is preferably 0 ⁇ A 2 ⁇ 30 mm, in particular 10 mm ⁇ A 2 ⁇ 30 mm.
  • the baffles are designed and arranged such that they face at least the dispersing blades. This means that the vertical extent of the baffles is so large that it corresponds at least to the height of the dispersing blades. This ensures that as many particles of the feed material leaving the dispersing plate are captured by the impact elements.
  • the sifter has a sifter wheel having sifter blades and an air guide system having guide vanes for supplying sifting air, an annular sifting space being arranged between the sifter wheel and the air guidance system.
  • Such classifiers are also referred to as Abweiseradsichter.
  • the vanes are in the viewing space protruding, extending in the vertical direction baffles.
  • This classifier does not have the dispersing plate and task cone according to the invention, but only the air-guiding system according to the invention.
  • the dispersing plate is preferably fastened to the classifier wheel.
  • the advantage is that the dispersing plate does not require its own drive and is driven by the classifier wheel.
  • the dispersing plate thus has the same angular velocity as the reformerrad.
  • the feed material in particular also the deagglomerated feedstock, tends to form strands in front of and in the viewing space which impair the classification.
  • Strands are understood to mean an accumulation of particles in a gas flow which, due to segregation, e.g. B. forms by the action of gravity and centrifugal force. Strands have their cause in exceeding the carrying capacity of the gas for the solid particles. In the strand thus smaller particles are included, which would otherwise arrive at low solids loadings with the flow of air into the fines.
  • baffles By projecting into the viewing space baffles a targeted loosening of the strands, so that an improved separation, in particular the finest particles is possible without affecting the rest of the deposition.
  • baffles By projecting into the viewing space baffles not only the strands are dissolved, but it is the particles of the feed material also imparted an additional component of movement in reformersrad direction.
  • the air duct system has air windows, wherein a baffle is arranged on at least one edge of the air window.
  • the air guidance system preferably has an annular wall in which the air windows are arranged.
  • the incoming air through the air windows is deflected by the baffles, whereby the flow is influenced in the viewing space.
  • the baffles thus fulfill two tasks. Both the particles of the feed material and the inflowing classifying air are influenced in the desired manner.
  • the angle of attack ⁇ of the baffles both flows can be adjusted specifically.
  • the angle of attack ⁇ is clamped between the baffles in the flow direction of the particle-air mixture in the viewing space and the inner radius R L of the air duct system.
  • the angles ⁇ are the same for all baffles.
  • the baffles are arranged on the opposite edges of the air window.
  • Each air window thus has two baffles, whereby the incoming air flow can be initiated more targeted.
  • the baffles between each two air windows are arranged such that their ends converge.
  • the baffles preferably have different angles of incidence ⁇ in this embodiment.
  • the ends of the baffles are preferably spaced, d. H. the ends of the baffles preferably do not touch.
  • each of the two baffles which are arranged on each air window, aligned parallel to each other.
  • These baffle pairs form an air channel, which preferably has a constant width.
  • the baffles with the radius R L of the air guidance system preferably have an angle of incidence ⁇ which is in the range of 30 ° to 60 °, particularly preferably in the range of 40 ° to 50 °.
  • the baffles are preferably rectangular planar guide elements.
  • the guide plates are curved in the direction of the classifier wheel.
  • the angle of attack ⁇ of the curved guide plate is clamped between the tangent T in the middle of the outer surface of the guide plate and the inner radius R L of the air-guiding system in the direction of flow of the particle air flow.
  • the flow direction of the particle air flow is defined by the direction of rotation of the classifier wheel.
  • the curved embodiment of the baffles has the advantage that the particle air flow is directed more effectively to the classifier wheel.
  • the baffles have a single radius of curvature R 4 .
  • the baffles are curved in such a way that the radius of curvature R 4 decreases in the direction of classifier wheel.
  • the radius of curvature is preferably 5 mm ⁇ R 4 ⁇ 2000 mm.
  • the air guidance system preferably has at least one cone ring with a particle guide element projecting into the viewing space and having a first cone-shaped surface.
  • the particle air flow has not only a horizontal component of motion, but also a vertical component of motion due to gravity.
  • the flow cross section of the viewing space in the vertical direction of movement is constricted by the cone ring, whereby the particle air flow is deflected by the cone-shaped surface of the particle guide element in the direction of bombarderrad. This measure also contributes to an improvement in the selectivity of the classifier.
  • the cone-shaped surface is arranged on the upper side of the particle guide element and forms with a vertical axis L V an angle ⁇ with 10 ° ⁇ ⁇ 90 °, particularly preferably 20 ° ⁇ ⁇ 80 °.
  • the ratio V of the diameter D L / D S is 1.05 ⁇ V ⁇ 1.1.
  • the air guidance system has at least one circumferential horizontal air slot.
  • This horizontal air slot may extend partially or over the entire circumference of the air handling system. This results in higher radial speeds of the classifier air of up to 30 m / s, with which the feed material is guided to the classifier wheel.
  • the classifier 1 has a housing 2 which has a filler pipe 6 and is divided into an upper housing part 3 and a lower housing part 5.
  • the upper housing part 3 which is formed substantially cylindrical, there is a sorterrad 60 with submiterrad 80 and the air guide system 70 with three Leitschaufelkränzen 72.
  • the conveyerrad 60 a dispersing plate 30 is fixed, thereby characterized by Classifier wheel 60 is driven.
  • the dispersing plate 30 has at its top 31 (see also FIG. 2 ) in the edge region of dispersing vanes 40, which consist of substantially rectangular metal platelets, which rise from the top 31 of the dispersing 30 and extend up to the edge 33 of the dispersing 30th About the dispersing a task cone 20 is fixedly attached to the housing 2.
  • the upper housing part 3 has a classifier cover 4, in which the filler pipe 6 is arranged with the filling opening 7 for the feed material.
  • the feed material is filled through the filler pipe 6 in the classifier 1 and meets there on the task cone 20th
  • the drive shaft 13 is arranged for the crusherrad 60, which is driven at the lower end by a drive device 12.
  • the lower housing part 5 also has an outlet pipe with the outlet opening 9 for discharging the fine material.
  • a suction fan 11 and the outlet 10 for the coarse material is arranged at the lower end of the conical lower housing part 5.
  • FIG. 2 shows a detail section through the upper portion of the housing 3rd
  • the task cone 20 projects with its conical tip 26 into the filler pipe 6 and is fastened there by means of a fastening element 22 to the filler neck 6.
  • the dispersing plate 30 is surrounded by a baffle ring 50, which has on its inner surface 52 baffle elements 54 which protrude in the direction of the dispersing plate 30 from the inner surface 52.
  • the baffles 54 are arranged distributed over the inner surface 52 of the baffle ring 50 and extend in the vertical direction at least over the entire height of the dispersing blades 40.
  • the baffle ring 50 is followed by a conical wall 58 at the top.
  • the classifying wheel 60 which is arranged underneath the dispersing disk 30, has a multiplicity of vertically oriented classifier wheel blades 62 and is surrounded by an air-guiding system 70 with a total of three guide-blade rings 72.
  • FIG. 3 is the top view on the in FIG. 1 shown separator 1, which has two tangentially arranged on the housing part 3 reformluftzu Replacementen 8a, b.
  • separator 1 which has two tangentially arranged on the housing part 3 submitluftzu Examinationen 8a, b.
  • the baffles 54 are arranged at a distance from the dispersing plate 30.
  • the dispersing plate 30 carries at its upper side 31 six dispersing blades 40, which partially extend below the task cone 20.
  • the inner periphery of the dispersing blades 40 is indicated by the dashed circle 44 on which the inner surfaces 41 of the dispersing blades 40 lie.
  • the corresponding radius R 3 of the inner circumference 44 of the dispersing blades 40 is also shown as the radius R 1 of the cone edge 24 of the task cone 20th
  • FIGS. 4 and 5 show enlarged sectional views of the upper part of in FIG. 2
  • the preparekegel 20 has an opening angle ⁇ of about 85 °.
  • the task cone 20 extends into the area of the dispersing blades 40, so that the feed material 14 introduced from above through the filler pipe 6 is supplied directly to the dispersing blades 40.
  • the agglomerates in the feed material 14 are identified by the reference numeral 15.
  • the agglomerates 15 as well as the other particles of the feedstock 14th are first detected by the dispersing surface 46 of the dispersing blades 40 before impacting the top surface 31 of the dispersing disk 30.
  • the radii R 1 , R 2 and R 3 are shown, wherein it can be seen that the radius R 3 is smaller than the radius R 1 , wherein for the radius is preferably 0.4 x R 2 ⁇ R 3 ⁇ 0.8 x R 2 . This ensures that the agglomerates 15 of the feed material 14 when leaving the task cone 20 do not overshoot the edge 33 of the dispersing plate 30 without hitting the dispersing blades 40.
  • the distance A 1 between the cone edge of the task cone 20 and the top surface 43 of the dispersing blade 40 is shown. Furthermore, the distance A 2 between the edge surface 34 of the dispersing plate and the impact element 56 is shown. The outer surface 42 of the dispersing blade 40 is set back relative to the edge surface 34 of the dispersing disk 30.
  • the impact element 54 extends below the level in which the underside 32 of the dispersing plate 30 lies.
  • the length L S of the dispersing blades 40 is preferably in the range of 0.02 ⁇ R 2 ⁇ L S ⁇ 0.2 ⁇ R 2 .
  • the height H S is preferably in the range of 0.01 ⁇ R 2 ⁇ H S ⁇ 0.1 ⁇ R 2 .
  • a 1 ⁇ R is 2/6.
  • A is preferably 1 ⁇ R 2/2.
  • the height H P of the baffle elements 54 are preferably 0.03 ⁇ R 2 ⁇ H P ⁇ 0.5 ⁇ R 2 applies.
  • the width B P of the impact element 54 is slightly less than the height H S of the dispersing blade 40.
  • an agglomerate particle 15 is shown, which slips down on the conical surface and is captured by the dispersing surface 46 and decomposed into its individual particles.
  • the resulting deagglomerated particles 16 strike the baffle 56 of the baffle 54 and are further deagglomerated there.
  • FIG. 6 the plan view of a separator wheel 60 with separator blades 62 and associated air guide system 70 having air vanes 73 are shown.
  • the vane ring 72 of the air control system 70 has an inner diameter D L.
  • the outer diameter of the reformerrades 60 is indicated by D S. This results in a width A 4 of the annular viewing space 18th
  • FIG. 7 a further embodiment of the air control system 70 is shown.
  • the air guidance system 70 has two rings 79, between which an annular wall 71 with air windows 74 is arranged.
  • the air windows 74 are arranged uniformly over the entire circumference of the annular wall 71.
  • In the embodiment shown here are rectangular air windows 74, each having at the left edge 75 air guide vanes 73 in the form of baffles 76.
  • These baffles 76 are pivotally mounted about an axis L SA , so that the angle of attack ⁇ , in the FIG. 9 is located, can be targeted.
  • FIG. 9 In the FIG. 9 is indicated in the viewing space 18 by the arrow P 2, the flow direction of the particle air flow, which is generated by the rotation of the prepareerrades 60 in the direction of the arrow P 1 .
  • the angle ⁇ is clamped between the inner radius R L of the air duct system 70 and the guide plate 76.
  • FIG. 8a In the FIG. 8a is the air duct 70 of the FIG. 7 shown combined with a crusherrad 60.
  • P 1 indicates the direction of rotation of the preparerrad 60.
  • P 2 With P 2 , the flow direction of the particle air flow is called.
  • FIG. 8b another embodiment is shown, in which the baffles 76 are curved.
  • the baffles 76 have a uniform radius of curvature R 4 and are curved in the direction detoxerrad.
  • the angle of attack ⁇ is indicated by the tangent T through the center of the baffle 76 and the inner radius of the air-directing system 70.
  • FIG. 8c a further embodiment is shown, in which the guide plates 76 have no uniform radius of curvature, but have a decreasing from outside to inside radius of curvature.
  • the radius of curvature R 6 at the end of the curved guide plate 76 is smaller than the radius of curvature R 5 .
  • FIG. 10 another embodiment of the air guide system 70 is shown, in each case at both edges 75 of the air window 74 opposite guide plates 77a, 77b are arranged.
  • the air inflow is indicated by the arrows. While the baffles 77a are formed short, the baffles 77b are made longer.
  • the adjacent baffles 77a and 77b of two windows 74 are each aligned in parallel, so that an air duct is provided with a constant width.
  • the ends 77c of the baffles 77a, 77b do not touch and are spaced from one another.
  • FIG. 11 a further embodiment of the air guide system 70 is shown in which three vane rings 72 are arranged one above the other, wherein between the rings 79 adjacent vane rings 72 each have a cone ring 80 is arranged.
  • a horizontal annular air slot 78 is provided in this air guide system 70 is introduced through the classifying air into the viewing space 18.
  • a cone ring 80 is shown in section.
  • the cone ring 80 has a particle guide element 82 having a first conical surface 84 at the top and a second conical surface 86 at the bottom.
  • the inclination angle of the surface 84 to a vertical axis L V is indicated by ⁇ .
  • the air guidance system 70 is shown together with a classifying wheel 60, so that it can be seen that the particle guide elements 82 project into the viewing space 18.
  • the distance A 3 from the inner edge 88 of the particle guide elements 84 to the classifier wheel is marked with A 3 .
  • the diameter D L and Ds and the distance A 4 between the air guide system 70 and the reformerrad 60 are located.
  • This powder was classified in a conventional classifier without task cone according to the invention and without dispersing plate according to the invention.
  • the same powder was in a sifter according to the invention with the task cone invention, dispersing with dispersing blades and a baffle ring according to the FIGS. 1 to 5 and an air-handling system according to FIG. 6 classified.
  • the sum distribution curve II obtained with the separator according to the invention is likewise shown in FIG. 14 shown.
  • the yield for this particle range was 7.3% in the prior art (curve I) and 11.3% with the classifier according to the invention (curve II). This is an increase of 54.8%.

Landscapes

  • Combined Means For Separation Of Solids (AREA)
  • Centrifugal Separators (AREA)
  • Filling Or Emptying Of Bunkers, Hoppers, And Tanks (AREA)
  • Cell Separators (AREA)
  • Cyclones (AREA)
EP18203588.1A 2016-04-11 2017-04-07 Séparateur Active EP3461565B1 (fr)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DE102016106588.9A DE102016106588B4 (de) 2016-04-11 2016-04-11 Sichter
PCT/EP2017/058430 WO2017178379A2 (fr) 2016-04-11 2017-04-07 Séparateur
EP17719819.9A EP3442721B1 (fr) 2016-04-11 2017-04-07 Tamiseur

Related Parent Applications (2)

Application Number Title Priority Date Filing Date
EP17719819.9A Division-Into EP3442721B1 (fr) 2016-04-11 2017-04-07 Tamiseur
EP17719819.9A Division EP3442721B1 (fr) 2016-04-11 2017-04-07 Tamiseur

Publications (2)

Publication Number Publication Date
EP3461565A1 true EP3461565A1 (fr) 2019-04-03
EP3461565B1 EP3461565B1 (fr) 2024-07-17

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EP18203588.1A Active EP3461565B1 (fr) 2016-04-11 2017-04-07 Séparateur
EP17719819.9A Active EP3442721B1 (fr) 2016-04-11 2017-04-07 Tamiseur

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EP17719819.9A Active EP3442721B1 (fr) 2016-04-11 2017-04-07 Tamiseur

Country Status (7)

Country Link
US (1) US11117167B2 (fr)
EP (2) EP3461565B1 (fr)
CN (2) CN108883437B (fr)
BR (1) BR112018071011A2 (fr)
DE (1) DE102016106588B4 (fr)
ES (2) ES2984648T3 (fr)
WO (1) WO2017178379A2 (fr)

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Publication number Priority date Publication date Assignee Title
US10744534B2 (en) * 2016-12-02 2020-08-18 General Electric Technology Gmbh Classifier and method for separating particles
WO2020066046A1 (fr) * 2018-09-26 2020-04-02 佐竹化学機械工業株式会社 Rotor de classification et dispositif de classification
DE102019123034B3 (de) * 2019-08-28 2020-12-03 Khd Humboldt Wedag Gmbh Zyklon mit rotierendem Stabkorb
WO2021099396A1 (fr) * 2019-11-22 2021-05-27 Gebr. Pfeiffer Se Roue de tamisage à éléments de voile plats
CN112794442B (zh) * 2021-01-22 2023-04-07 重庆市巴南排水有限责任公司 一种基于生化处理工艺的碳源投加装置及投加方法
DE102021001238B4 (de) 2021-03-09 2023-01-26 Hosokawa Alpine Aktiengesellschaft Zentrifugalkraft-Windsichter und Verfahren zur Sichtung von staubförmigen Gütern

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DE3823380C2 (de) 1988-07-09 1994-09-08 Kloeckner Humboldt Deutz Ag Sichter zum Sichten von körnigem, insbesondere agglomeriertem Gut
EP0645196A1 (fr) * 1993-03-31 1995-03-29 Onoda Cement Company, Ltd. Separateur a air a tourbillon
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EP2204240A1 (fr) * 2007-09-27 2010-07-07 Babcock-Hitachi Kabushiki Kaisha Dispositif de classification, pulvérisateur vertical utilisant le dispositif de classification, et appareil de chaudière à charbon
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DE102016106588B4 (de) 2023-12-14
CN108883437A (zh) 2018-11-23
CN108883437B (zh) 2022-07-15
EP3442721B1 (fr) 2023-05-24
CN113042368A (zh) 2021-06-29
EP3461565B1 (fr) 2024-07-17
US11117167B2 (en) 2021-09-14
ES2984648T3 (es) 2024-10-30
US20190168263A1 (en) 2019-06-06
EP3442721A2 (fr) 2019-02-20
DE102016106588A1 (de) 2017-10-12
WO2017178379A3 (fr) 2017-12-07
WO2017178379A2 (fr) 2017-10-19
ES2949867T3 (es) 2023-10-03
BR112018071011A2 (pt) 2019-02-12

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