EP2782679B1 - Centrifugeuse discontinue comprenant un panier rotatif pourvu d'une enveloppe et procédé de fabrication de cette enveloppe - Google Patents

Centrifugeuse discontinue comprenant un panier rotatif pourvu d'une enveloppe et procédé de fabrication de cette enveloppe Download PDF

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Publication number
EP2782679B1
EP2782679B1 EP12788582.0A EP12788582A EP2782679B1 EP 2782679 B1 EP2782679 B1 EP 2782679B1 EP 12788582 A EP12788582 A EP 12788582A EP 2782679 B1 EP2782679 B1 EP 2782679B1
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EP
European Patent Office
Prior art keywords
holes
casing
centrifuge
cross
drum
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.)
Active
Application number
EP12788582.0A
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German (de)
English (en)
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EP2782679A1 (fr
Inventor
Hans-Heinrich Westendarp
Dirk SPANGENBERG
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.)
BMA Braunschweigische Maschinenbauanstalt AG
Original Assignee
BMA Braunschweigische Maschinenbauanstalt AG
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Publication date
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Publication of EP2782679A1 publication Critical patent/EP2782679A1/fr
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Publication of EP2782679B1 publication Critical patent/EP2782679B1/fr
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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04B—CENTRIFUGES
    • B04B11/00—Feeding, charging, or discharging bowls
    • B04B11/04—Periodical feeding or discharging; Control arrangements therefor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04B—CENTRIFUGES
    • B04B7/00—Elements of centrifuges
    • B04B7/02—Casings; Lids
    • B04B7/04—Casings facilitating discharge
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04B—CENTRIFUGES
    • B04B13/00—Control arrangements specially designed for centrifuges; Programme control of centrifuges
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04B—CENTRIFUGES
    • B04B3/00—Centrifuges with rotary bowls in which solid particles or bodies become separated by centrifugal force and simultaneous sifting or filtering
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04B—CENTRIFUGES
    • B04B7/00—Elements of centrifuges
    • B04B7/08—Rotary bowls
    • B04B7/12—Inserts, e.g. armouring plates
    • B04B7/14—Inserts, e.g. armouring plates for separating walls of conical shape
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04B—CENTRIFUGES
    • B04B7/00—Elements of centrifuges
    • B04B7/08—Rotary bowls
    • B04B7/12—Inserts, e.g. armouring plates
    • B04B7/16—Sieves or filters
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04B—CENTRIFUGES
    • B04B7/00—Elements of centrifuges
    • B04B7/08—Rotary bowls
    • B04B7/18—Rotary bowls formed or coated with sieving or filtering elements
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B26—HAND CUTTING TOOLS; CUTTING; SEVERING
    • B26F—PERFORATING; PUNCHING; CUTTING-OUT; STAMPING-OUT; SEVERING BY MEANS OTHER THAN CUTTING
    • B26F3/00—Severing by means other than cutting; Apparatus therefor
    • B26F3/004—Severing by means other than cutting; Apparatus therefor by means of a fluid jet

Definitions

  • the invention relates to a discontinuous centrifuge with a drum rotating about a drum centrifuge drum with a jacket in which the cylindrical centrifuge shell is provided with holes for the flow of a liquid formed during centrifugation, which holes have a cross-section with an elliptical shape,
  • the invention also relates to a method for producing a jacket for such a discontinuous centrifuge. Furthermore, the invention relates to a method for operating such a discontinuous centrifuge.
  • a centrifugal separator with radial openings according to the preamble of claim 1 is known from EP 0 804 291 B1 according to the DE 696 09 594 T2 known.
  • the rotor of the centrifugal separator is constructed with passages in the form of the radial openings so that in the radial passages the risk of blockages or wear is reduced and that by a special design of the cross section of the passages a reduction of the generated noise level and an influence on the Frequencies of the sound generated in the passages occurs.
  • the passage is formed so that its radially inner cross section is initially constant or slowly increases outwardly and then jumps discontinuously outwards in the middle of the passage.
  • Discontinuous centrifuges are also used in particular for the separation of sugar crystals from sugar crystal suspensions.
  • a feedstock is supplied, for example, a magma with enriched crystal suspensions, and then treated in the centrifuge drum so as to be deposited on the inner surface of a jacket of the centrifuge drum a product, for example, here a crystals, settles.
  • the syrup exits through a working sieve, which lies on the mantle.
  • Such a design also known as periodic centrifuge for throwing off fillers is already known from the DE 1 916 280 B known. Holes are provided in the centrifuge shell, through which the liquid separated from the sugar crystals during centrifugation is discharged to the outside and leaves the centrifuge drum.
  • the object of the invention is therefore to propose a discontinuous centrifuge which has a further optimization of the centrifuge shell.
  • Another object of the invention is to provide a method for producing such a centrifuge.
  • the first object is achieved in a generic discontinuous centrifuge by means of the invention in that the cross section of the holes is continuous from the inside out that the diameter (a 2 ) of the cross sections of the holes parallel to the drum axis on the inside of the shell is equal to or nearly equal to the diameter (a 1 ) of the cross sections of the holes parallel to the drum axis on the outside of the holes and in that the diameter (I 2 ) of the cross sections of the circumferential holes on the inside of the shell is smaller than the diameter (I 1 ) of the cross sections of the circumferential holes on the outside of the shell, so that the cross sections of the holes expand outwardly.
  • the object is achieved by means of the invention in that the jacket is provided before or after the rounding of the jacket plate by means of water jet cutting with openings in elliptical shape.
  • the opening area should become larger toward the outside. At the same time, a larger area is advantageous against which the liquid can "lean".
  • the diameter of the cross sections of the holes parallel to the drum axis on the inside of the shell should be equal to the diameter of the cross sections of the holes parallel to the drum axis on the outside of the holes, it is understood that these two diameters are less than 5% of each other should differ. A slight deviation, in particular a slight extension of the cross section to the outside in this dimension is still tolerable, although it should be as low as possible.
  • the expansion of the cross-sections from the inside to the outside is by one dimension in the circumferential direction of the centrifuge drum, ie at the same time in the direction of movement of a rotating drum.
  • the wall of the hole should therefore be designed differently in the different areas of the hole wall.
  • the holes are introduced by means of a water jet cut before the rounding of the sheet to form the cylindrical centrifuge shell as openings in a cladding sheet.
  • an ellipse with running parallel to the drum axis web in the middle can be realized, which divides the ellipse into two halves symmetrical to each other.
  • This has the advantage that with the web additional surface is created, which additionally accelerates the liquid and therefore the liquid leaves the drum faster.
  • the web surface is also slightly sloping outward in the direction of rotation here.
  • the inventive design of the centrifuge shell can still use another effect.
  • the cross-sectional shape of the holes in the form of an ellipse favors a centering opening surface, which then fewer holes are required in total.
  • the ellipse has a multiple of area compared to a hole having a circular cross section at the same dimension in the axis-parallel direction. For a smaller number of holes, fewer separate manufacturing steps are needed. Accordingly, for the forwarding and further processing of the fluids passing through the elliptical holes, fewer positions have to be taken into account, at which the fluids emerge on the outside of the centrifuge drum.
  • the centrifuge drum 10 has a drive spindle 11, which also forms the vertically arranged axis of the centrifuge drum 10 and provides the rotary drive for the entire centrifuge drum 10.
  • the drive spindle 11 is indicated only schematically.
  • the direction of rotation 12 is additionally marked by an arrow.
  • the centrifuge drum 10 also has a jacket 13 which is rotated by the rotary drive 11 in a rotational movement.
  • the jacket 13 is substantially cylindrical and covered on its inner wall by a not-shown working screen.
  • the sugar crystals remain on the inside of the jacket 13 in the form of a crystallizate 14 and form a kind of sugar layer there.
  • the bottom 15 is arranged substantially perpendicular to the axis of the centrifuge drum 10. However, the bottom 15 has openings 16 through which the crystals 14 can escape from the centrifuge drum 10 due to its gravity. These openings 16 are closed during the centrifuging process and are only then opened.
  • the scraper 20 has a scraper bar 21 and an element 22 arranged on the scraper bar 21, for example a paring knife 22 or a razor.
  • the paring knife 22 or the Räumpflug are pivotable relative to the raking bar about the axis formed by the raking bar 21.
  • the peeling blade 22 and the Räumpflug parallel to the axis of the centrifuge drum 10 and thus vertically. They extend over the whole or almost the entire height of the shell 13th
  • This pivotal movement causes the paring knife 22 to move into the crystals 14 and successively peels off the layers of the crystals 14 there.
  • the scraper 20 is supplemented with its clearing bar 21 by an element 22 in the form of a paring knife or Räumflugs. In the position shown, this element 22 does not reach into the crystallizate 14. This position from the FIG. 1 and the FIG. 2 is thus taken during centrifugation.
  • the jacket 13 is provided with a larger number of holes 50. These holes 50 are in proportion so small that they in the illustration in the Figures 1 and 2 do not appear separately.
  • FIG. 3 is a jacket plate shown that for the production of a shell 13 from the Figures 1 and 2 would be suitable.
  • the holes 50 are thereby introduced by means of water jet cutting in the jacket plate for the jacket 13.
  • FIG. 4 one can see a first embodiment of a hole 50 at the top in the section and at the bottom in a plan view.
  • a hole 50 at the top in the section and at the bottom in a plan view.
  • the FIG. 4 is above the jacket plate for the jacket 13 in section and below the area of the hole 50 in plan view to recognize.
  • the hole 50 has an elliptical shape and is introduced into the jacket sheet by abrasive processes perpendicular to the plane of the sheet.
  • FIG. 5 one sees a second embodiment of a hole 50 at the top in the section and at the bottom in a plan view.
  • the hole 50 is here composed of two individual regions 50a and 50b, which together form an elliptical shape with an intermediate web 51.
  • the web is advantageously already produced slightly obliquely (viewed in plan view) and although continuously sloping outwardly in the direction of rotation.
  • FIG. 6 A third embodiment of a hole 50 at the top in section and at the bottom in a plan view can be seen.
  • the hole 50 is here in turn elliptical and divided by two webs 51a and 51b, so that three partial holes 50a, 50b and 50c are formed.
  • FIG. 7 is a plan view of an embodiment of a hole 50 is shown, the first of the representation in the FIG. 4 similar.
  • the hole 50 has a total of three dimensions.
  • a first dimension runs on the circumference of the cylinder drum and is in the FIG. 7 to recognize in the leaf level from left to right.
  • a second dimension runs on the cylinder drum parallel to the drum axis and is in the sheet plane in the FIG. 7 shown from top to bottom.
  • a third dimension is perpendicular to the jacket 13 of the centrifuge drum 10 and thus is perpendicular to the sheet plane in the FIG. 7 ,
  • the jacket 13 of the centrifuge drum has a finite dimension. It has an inner side facing the drum axis and an outer side facing the environment.
  • the hole 50 now has a cross section, which is constructed elliptical in each case.
  • the elliptical cross-section thus has a usually smaller diameter, which in the illustrated embodiment is parallel to the drum axis, in the FIG. 7 So from top to bottom.
  • a 1 denotes the diameter of the elliptical cross-section on the outside of the jacket 13
  • a 2 the diameter of the elliptical cross-section on the inside of the jacket 13.
  • both diameters a 1 and a 2 are the same and also fall each other.
  • the second, in the majority of embodiments and also in the illustrated embodiment larger diameter is perpendicular to the first diameters a 1 and a 2 in the circumferential direction of the shell 13 and thus in the FIG. 7 left to right.
  • the cross section of the elliptical hole 50 located on the outside of the drum shell is denoted by I 1
  • the diameter of the elliptical cross section located on the inside of the casing 13 in this dimension is denoted by I 2 .
  • I 1 is greater than I 2 . Since the hole wall, the ellipse-like cross-sections on the outside of the jacket 13 and inside the shell 13 connects steadily, it follows that the hole wall in the FIG. 7 on the sides, which are in the illustration above or below, perpendicular to the sheet plane, while in the areas that are located to the left or right of the hole 50, obliquely to the sheet plane.

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  • Life Sciences & Earth Sciences (AREA)
  • Forests & Forestry (AREA)
  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Centrifugal Separators (AREA)

Claims (15)

  1. Centrifugeuse discontinue
    comprenant un tambour de centrifugeuse (10) pouvant tourner autour d'un axe de tambour et pourvu d'une enveloppe (13),
    dans laquelle l'enveloppe de centrifugeuse cylindrique (13) est pourvue de trous (50) pour l'écoulement d'un liquide produit lors de la centrifugation, lesquels trous (50) possèdent une section transversale de forme elliptique, le diamètre (I2) des sections transversales des trous (50) dans la direction circonférentielle étant plus petit du côté intérieur de l'enveloppe (13) que le diamètre (I1) des sections transversales des trous (50) dans la direction circonférentielle du côté extérieur de l'enveloppe (13), de sorte que les sections transversales des trous (50) s'élargissent vers l'extérieur,
    caractérisée en ce
    que la section transversale des trous (50) est continue de l'intérieur vers l'extérieur,
    que le diamètre (a2) des sections transversales des trous (50) parallèlement à l'axe de tambour du côté intérieur de l'enveloppe (13) est égal ou sensiblement égal au diamètre (a1) des sections transversales des trous (50) parallèlement à l'axe de tambour du côté extérieur des trous (50).
  2. Centrifugeuse discontinue selon la revendication 1,
    caractérisée en ce
    que les sections transversales elliptiques s'élargissant vers l'extérieur des trous (50) présentent des parois de trou faisant un angle de plus de 0,1° et de moins de 10°, de préférence de plus de 0,2° et de moins de 3° par rapport à la perpendiculaire à l'enveloppe (13) aux extrémités extérieures du diamètre (I1, I2) dans la direction circonférentielle.
  3. Centrifugeuse discontinue selon la revendication 1 ou 2,
    caractérisée en ce
    que les parois de trou des trous (50) sont aussi continues dans la direction circonférentielle.
  4. Centrifugeuse discontinue selon l'une des revendications précédentes,
    caractérisée en ce
    que les trous (50) sont réalisés sous la forme d'ouvertures dans une tôle d'enveloppe au moyen d'une coupe à hydrojet avant le cintrage de la tôle pour former l'enveloppe de centrifugeuse cylindrique (13).
  5. Centrifugeuse discontinue selon l'une des revendications précédentes,
    caractérisée en ce
    que le diamètre (I1, I2) des sections transversales des trous elliptiques (50) dans la direction circonférentielle est plus grand que le diamètre (a1, a2) des trous (50) parallèlement à l'axe de tambour, et
    que le rapport des demi-axes des ellipses est compris entre 1:2,5 et 1:7,5, de préférence entre 1:4,5 et 1:5,5.
  6. Centrifugeuse discontinue selon l'une des revendications précédentes,
    caractérisée en ce
    que la surface ouverte de chaque ellipse est comprise entre 80 mm2 et 150 mm2, de préférence entre 95 mm2 et 105 mm2.
  7. Centrifugeuse discontinue selon l'une des revendications précédentes,
    caractérisée en ce
    que les trous (50) dans l'enveloppe (13) du tambour de centrifugeuse (10) présentent une section d'ouverture différente répartie sur la hauteur du tambour.
  8. Centrifugeuse discontinue selon l'une des revendications précédentes,
    caractérisée en ce
    que les trous (50) dans l'enveloppe (13) du tambour de centrifugeuse (10) présentent des distances mutuelles ou écarts mutuels différents sur la hauteur du tambour.
  9. Centrifugeuse discontinue selon l'une des revendications précédentes,
    caractérisée en ce
    que l'épaisseur de matériau de la tôle d'enveloppe de l'enveloppe (13) du tambour de centrifugeuse (10) est comprise entre 8 mm et 25 mm, de préférence entre 10 mm et 17 mm.
  10. Centrifugeuse discontinue selon l'une des revendications précédentes,
    caractérisée en ce
    qu'une, plusieurs ou toutes les ellipses des trous (50) dans l'enveloppe (13) du tambour de centrifugeuse (10) présentent au milieu au moins une traverse (51) s'étendant parallèlement à l'axe de tambour, laquelle divise de préférence l'ellipse en deux moitiés égales symétriques l'une par rapport à l'autre.
  11. Centrifugeuse discontinue selon la revendication 10,
    caractérisée en ce
    que la surface en section transversale des traverses (51) va en diminuant vers l'extérieur, et
    que la paroi de trou est aussi continue dans la zone des traverses (51).
  12. Centrifugeuse discontinue selon la revendication 10 ou 11,
    caractérisée en ce
    que l'ellipse présente plusieurs traverses (51a, 51b), de préférence au moins deux et au plus cinq.
  13. Procédé de fabrication d'une centrifugeuse discontinue comprenant un tambour de centrifugeuse (10) et une enveloppe (13) selon l'une des revendications précédentes,
    caractérisée en ce
    que l'enveloppe (13) est pourvue, avant le cintrage de la tôle d'enveloppe, au moyen d'une coupe à hydrojet, d'ouvertures de forme elliptique à partir desquelles, après le cintrage, sont formés les trous (50) de section transversale elliptique.
  14. Procédé de fabrication d'une centrifugeuse discontinue selon la revendication 13,
    caractérisée en ce
    que les ouvertures de forme elliptique reçoivent une forme conique au moyen d'une coupe à hydrojet avant le cintrage de la tôle d'enveloppe.
  15. Procédé de fabrication d'une centrifugeuse discontinue comprenant un tambour de centrifugeuse (10) et une enveloppe (13) selon l'une des revendications 1 à 12,
    caractérisée en ce
    que l'enveloppe (13) est pourvue de trous (50) ayant une section transversale de forme elliptique après le cintrage de la tôle d'enveloppe au moyen d'une coupe à hydrojet,
    que les parois des trous (50) sont continues de l'intérieur vers l'extérieur et dans la direction circonférentielle, et
    que le diamètre (I2) des sections transversales des trous (50) dans la direction circonférentielle est plus petit du côté intérieur de l'enveloppe (13) que le diamètre (I1) des sections transversales des trous (50) dans la direction circonférentielle du côté extérieur de l'enveloppe (13), de sorte que les sections transversales des trous (50) s'élargissent vers l'extérieur.
EP12788582.0A 2011-11-24 2012-11-23 Centrifugeuse discontinue comprenant un panier rotatif pourvu d'une enveloppe et procédé de fabrication de cette enveloppe Active EP2782679B1 (fr)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DE102011119262 2011-11-24
DE102012002351A DE102012002351A1 (de) 2011-11-24 2012-02-08 Diskontinuierliche Zentrifuge mit einer drehbaren Zentrifugentrommel mit einem Mantel und Verfahren zur Herstellung des Mantels
PCT/EP2012/073464 WO2013076243A1 (fr) 2011-11-24 2012-11-23 Centrifugeuse discontinue comprenant un panier rotatif pourvu d'une enveloppe et procédé de fabrication de cette enveloppe

Publications (2)

Publication Number Publication Date
EP2782679A1 EP2782679A1 (fr) 2014-10-01
EP2782679B1 true EP2782679B1 (fr) 2015-09-16

Family

ID=48287975

Family Applications (1)

Application Number Title Priority Date Filing Date
EP12788582.0A Active EP2782679B1 (fr) 2011-11-24 2012-11-23 Centrifugeuse discontinue comprenant un panier rotatif pourvu d'une enveloppe et procédé de fabrication de cette enveloppe

Country Status (8)

Country Link
US (1) US9463475B2 (fr)
EP (1) EP2782679B1 (fr)
CN (1) CN103648654B (fr)
BR (1) BR112014001481B1 (fr)
DE (1) DE102012002351A1 (fr)
MX (1) MX345190B (fr)
RU (1) RU2587087C2 (fr)
WO (1) WO2013076243A1 (fr)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2019076474A1 (fr) 2017-10-16 2019-04-25 Andritz Fiedler Gmbh Centrifugeuse à fonctionnement discontinu
RU191345U1 (ru) * 2019-03-01 2019-08-01 Федеральное государственное бюджетное образовательное учреждение высшего образования "Волгоградский государственный технический университет" (ВолгГТУ) Вертикальная центрифуга

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Publication number Priority date Publication date Assignee Title
DE102011119265B4 (de) * 2011-11-24 2018-01-04 Bma Braunschweigische Maschinenbauanstalt Ag Diskontinuierliche Zentrifuge mit Ausräumer zum Ausräumen eines Produktes
EP3643189B1 (fr) * 2018-10-25 2021-04-28 Shenzhen IVPS Technology Co., Ltd. Dispositif d'atomisation et cigarette électronique le comprenant

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DE1632291B1 (de) 1966-10-22 1971-07-29 Hitachi Shipbuilding Eng Co Kontinuierlich arbeitende Siebzentrifuge
DE1916280B1 (de) * 1969-03-29 1970-06-04 Buckau Wolf Maschf R Periodisch arbeitende Zentrifuge zum Abschleudern von Fuellmasse
GB1450634A (en) * 1974-05-24 1976-09-22 Braunschweigische Masch Bau Centrifuge for the continuous separation of solids from fluids
SE8006732L (sv) * 1980-09-26 1982-03-27 Alfa Laval Ab Anordning for att overvaka separerat sediment, som kastas ut genom munstycken hos en centrifugalseparator
RU2039609C1 (ru) * 1994-01-25 1995-07-20 Анатолий Владимирович Долгов Центрифуга для разделения суспензии
DE59401399D1 (de) * 1994-04-08 1997-02-06 Braunschweigische Masch Bau Verfahren zur Fest-Flüssig-Extrahierung und Extraktionsturm zur Durchführung des Verfahrens
SE505385C2 (sv) * 1995-11-17 1997-08-18 Alfa Laval Ab Rotor för en centrifugalseparator
NL1013880C2 (nl) * 1999-12-17 2001-06-21 Henk Dijkman Werkwijze voor het bedrijven van een waterstraalsnijinrichting en spuitmond voor een waterstraalsnijinrichting.
US6440316B1 (en) * 2000-03-21 2002-08-27 Virginia Tech Intellectual Properties, Inc. Methods of improving centrifugal filtration
US20040000734A1 (en) * 2002-06-28 2004-01-01 Ucar Carbon Company Inc. Centrifugal casting of graphite for rigid insulation
DE502005003446D1 (de) * 2005-02-18 2008-05-08 Braunschweigische Maschb Ansta Zentrifugentrommel sowie Zentrifuge und Verfahren zu deren Herstellung
DE102006053491A1 (de) * 2006-11-14 2008-05-15 Westfalia Separator Ag Zentrifuge, insbesondere Separator, mit Feststoff-Austrittsdüsen
GB0724572D0 (en) * 2007-12-17 2008-01-30 Specialist Process Technologie A separation device

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2019076474A1 (fr) 2017-10-16 2019-04-25 Andritz Fiedler Gmbh Centrifugeuse à fonctionnement discontinu
RU191345U1 (ru) * 2019-03-01 2019-08-01 Федеральное государственное бюджетное образовательное учреждение высшего образования "Волгоградский государственный технический университет" (ВолгГТУ) Вертикальная центрифуга

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BR112014001481A2 (pt) 2017-02-14
US20140256529A1 (en) 2014-09-11
CN103648654B (zh) 2017-05-31
BR112014001481B1 (pt) 2022-09-06
MX2014006058A (es) 2014-08-08
US9463475B2 (en) 2016-10-11
RU2587087C2 (ru) 2016-06-10
RU2014118498A (ru) 2015-12-27
MX345190B (es) 2017-01-20
WO2013076243A1 (fr) 2013-05-30
CN103648654A (zh) 2014-03-19
DE102012002351A1 (de) 2013-05-29
EP2782679A1 (fr) 2014-10-01

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