EP2326427B1 - Centrifuge having a selfdischarging bowl - Google Patents
Centrifuge having a selfdischarging bowl Download PDFInfo
- Publication number
- EP2326427B1 EP2326427B1 EP09783343.8A EP09783343A EP2326427B1 EP 2326427 B1 EP2326427 B1 EP 2326427B1 EP 09783343 A EP09783343 A EP 09783343A EP 2326427 B1 EP2326427 B1 EP 2326427B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- closing chamber
- recesses
- closing
- drum
- piston slide
- 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
Links
- 239000007787 solid Substances 0.000 claims description 8
- 239000012530 fluid Substances 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 18
- 238000010276 construction Methods 0.000 description 6
- 238000002347 injection Methods 0.000 description 5
- 239000007924 injection Substances 0.000 description 5
- 238000004140 cleaning Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000009795 derivation Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B1/00—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
- B04B1/10—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with discharging outlets in the plane of the maximum diameter of the bowl
- B04B1/14—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with discharging outlets in the plane of the maximum diameter of the bowl with periodical discharge
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B1/00—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
- B04B1/10—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with discharging outlets in the plane of the maximum diameter of the bowl
- B04B1/14—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with discharging outlets in the plane of the maximum diameter of the bowl with periodical discharge
- B04B1/16—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with discharging outlets in the plane of the maximum diameter of the bowl with periodical discharge with discharging outlets controlled by the rotational speed of the bowl
- B04B1/18—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with discharging outlets in the plane of the maximum diameter of the bowl with periodical discharge with discharging outlets controlled by the rotational speed of the bowl controlled by the centrifugal force of an auxiliary liquid
Definitions
- the invention relates to a centrifuge with a self-cleaning centrifugal drum according to the preamble of claim 1.
- a centrifuge with a self-cleaning centrifugal drum is from the DE-OS 19 09 996 known. Further developed constructions show the DE 32 08 808 A1 , the DE 32 40 093 A1 , the DE 35 09 139 C1 , the DE 35 24 731 C1 and the DE 36 07 526 A1 , With the known - known under the name Hydrostop - solutions can be particularly precise control part discharges, but it is in each case relatively expensive constructions.
- the object of the invention is to create a centrifuge optimized with regard to its emptying behavior with simple structural means.
- the construction according to the invention achieves an optimized emptying behavior with simple constructional means, which is in particular due to a rapidly initiated and relatively large evacuation stroke and a rapidly initiated one Signs closing, which leads to a rapid reduction of Austragsspalt Theory.
- a processed material to be processed - a solid-liquid mixture - is through a central inlet 22 (see insofar as the schematically illustrated construction of Fig. 4 ) is supplied to a rotatable drum 1 of a (plate) separator with a vertical axis of rotation, which has a centrifugal space 2, which is divided into a separation space 3 and a solid space 4.
- the solid space 4 is on one side - down here - limited by an axially movable piston slide 5, which releases or closes during its axial movements in the drum shell 6 ejection openings 7 for the solids.
- closing liquid can be introduced through an injection chamber 9 and a supply line.
- This closing fluid can be switched by one or more leads 11, in which one or more piston valves 12 are discharged from the drum 1, to which the piston valve 12 is acted upon by opening water, which is passed through an injection chamber 13 for opening water and a supply line 14 to the piston valve 12.
- the function of such a piston valve 12 is known per se in the field of self-draining separators.
- Opening water and closing water are sprayed by means of control water supply lines 22a, b through two separate water supply lines into the injection chambers 13 and 9, respectively, into the drum.
- valve piston moves outward (by the centrifugal force) and closes the bore 11.
- the spool 5 moves up again , which closes the drum 1.
- the closing chamber height that is to say the distance between the inner wall of the drum and the spool in the region of the closing chamber 8, is kept relatively low, preferably the height is 0.3 mm to 5 mm, in particular 0.5 to 1.5 mm.
- the volume of closed water is kept low.
- the height of the chamber significantly affects the rate of evacuation.
- a defined increment of the lock chamber 8 is set to a predetermined diameter of the lock chamber.
- the height of the closing chamber 8 multiplies in the region of this step jump preferably the height of the closing chamber 8 in the region of the recesses 17 is three to fifteen times the gap height of the closing chamber 8 in the area adjacent to or outside of the recesses 17, in particular 3 to 20 mm, more preferably 5 to 12 mm, in particular 10 mm.
- this increment is introduced in the region of the lower part of the piston slide.
- This reversal range of the angle of the spool is usually - viewed from the outside diameter of the spool - between one third and two thirds of its radius.
- the spool has here on its underside in its inner and outer edge region circumferential free rotations 20, 21 for better acceptance and for better removal of the closing water.
- the invention can be realized, for example, in a simple manner in that recesses 17 are introduced into the side of the piston slide 6 facing the closing chamber at a certain diameter, for example two or more cutouts distributed around the circumference.
- the recesses 17 lead to an optimized emptying behavior, as exemplified in Fig. 2 is shown.
- the cutouts 17 are designed depending on the nature of the product to be processed and the emptying (Teilentle mecanicge) to be carried out, which can be done for example empirically by means of experiments until a characteristic of the type Fig. 2 with a relatively large, fast to a maximum value increasing opening stroke and a relatively fast stopping the emptying results.
- the spool of the Fig. 1 has starting from a radius R17 in the region of the cutouts radially inwardly and outwardly double conical shape, wherein the cutouts 17 are formed in the transition region 17 between the two conical regions 18 and 19 by way of example as two variants.
- the comparison of the emptying characteristics as shown in Fig. 2 and 3 was carried out by way of example with a separator of the type MSD 300 of the Applicant.
- the lifting height of 100% refers to the mechanically realizable possibility of movement of the piston slide between the drum cover and the drum base.
- the time base of, for example, 1 sec refers to the control of the upstream solenoid valve for supplying the opening water.
Landscapes
- Centrifugal Separators (AREA)
Description
Die Erfindung betrifft eine Zentrifuge mit einer selbstentleerenden Schleudertrommel nach dem Oberbegriff des Anspruchs 1.The invention relates to a centrifuge with a self-cleaning centrifugal drum according to the preamble of claim 1.
Eine Zentrifuge mit einer selbstentleerenden Schleudertrommel ist aus der
Es ist auch bekannt, Kolbenventile zum zeitweisen Öffnen einer Schließkammer mit Hilfe einer außerhalb der Trommel angeordneten Dosiereinrichtung anzusteuern. Das Entleerungsverhalten derartiger Konstruktionen ist aber trotz der Dosiergeräte nicht immer optimal, da kein sehr großer Öffnungshub des Kolbenschiebers erreicht wird (siehe Fig- 3). Zudem bedingen die eingesetzten Dosiereinrichtungen einen erhöhten Kostenaufwand.It is also known to control piston valves for the temporary opening of a closing chamber by means of a metering device arranged outside the drum. The emptying behavior of such constructions, however, is not always optimal despite the metering devices, since no very large opening stroke of the piston valve is achieved (see FIG. 3). In addition, the dosing devices used require an increased cost.
Wünschenswert ist insofern ein schneller und auch großer Öffnungshub des Kolbenschiebers, um einen guten und gleichmäßigen Feststoffaustrag auch bei der Verarbeitung von weniger fließfähigen Feststoffen zu ermöglichen.In this respect, it is desirable to have a fast and also large opening stroke of the spool valve in order to enable a good and uniform discharge of solids even when processing less free-flowing solids.
Zum Stand der Technik seinen ergänzend noch die
Die Erfindung hat vor diesem Hintergrund die Aufgabe, mit einfachen konstruktiven Mitteln eine hinsichtlich ihres Entleerungsverhaltens optimierte Zentrifuge zu schaffen.Against this background, the object of the invention is to create a centrifuge optimized with regard to its emptying behavior with simple structural means.
Die Erfindung löst diese Aufgabe durch den Gegenstand des Anspruchs 1.The invention solves this problem by the subject matter of claim 1.
Die erfindungsgemäße Konstruktion erreicht mit einfachen konstruktiven Mitteln ein optimiertes Entleerungsverhalten, das sich insbesondere durch einen schnell eingeleiteten und relativ großen Entleerungshub und einen schnell eingeleiteten Schließvorgang auszeichnet, der zu einer raschen Verkleinerung der Austragsspalthöhe führt.The construction according to the invention achieves an optimized emptying behavior with simple constructional means, which is in particular due to a rapidly initiated and relatively large evacuation stroke and a rapidly initiated one Signs closing, which leads to a rapid reduction of Austragsspalthöhe.
Vorteilhafte Ausgestaltungen der Erfindung sind den Unteransprüchen zu entnehmen.Advantageous embodiments of the invention can be found in the dependent claims.
Nachfolgend wird die Erfindung unter Bezug auf die Zeichnung näher beschrieben. Es zeigen:
- Fig. 1
- einen Schnitt durch einen Teilbereich einer erfindungsgemäßen Schleudertrommel;
- Fig. 2
- ein Diagramm, welches den Hub des Kolbenschiebers über die Zeit mit einer Schleudertrommel nach Art der
Fig. 1 darstellt; - Fig. 3
- ein Diagramm, welches den Hub des Kolbenschiebers über die Zeit mit einer bekannten Schleudertrommel darstellt; und
- Fig. 4
- eine schematisch schnittartig dargestellte, weitere erfindungsgemäße Schleudertrommel.
- Fig. 1
- a section through a portion of a centrifugal drum according to the invention;
- Fig. 2
- a diagram showing the stroke of the piston valve over time with a centrifugal drum in the manner of
Fig. 1 represents; - Fig. 3
- a diagram illustrating the stroke of the spool valve over time with a known centrifugal drum; and
- Fig. 4
- a schematically illustrated in section, another centrifugal drum according to the invention.
Ein zu verarbeitendes Schleudergut - ein Feststoff-Flüssigkeitsgemisch - wird durch einen mittigen Einlauf 22 (siehe insoweit die schematisch dargestellte Konstruktion der
Der Feststoffraum 4 wird einseitig - hier nach unten hin - von einem axial beweglichen Kolbenschieber 5 begrenzt, der bei seinen axialen Bewegungen im Trommelmantel 6 ausgebildete Auswurföffnungen 7 für die Feststoffe freigibt bzw. verschließt.The solid space 4 is on one side - down here - limited by an axially
Zwischen dem Kolbenschieber 5 und dem Trommelmantel 6 bzw. dem Trommelunterteil ist eine mit Schließfluid beaufschlagbare Schließkammer 8 ausgebildet.Between the
In die Schließkammer 8 kann durch eine Einspritzkammer 9 und eine Zuleitung 10 Schließflüssigkeit eingeleitet werden. Diese Schließflüssigkeit kann durch eine oder mehrere Ableitungen 11, in die eines oder mehrere Kolbenventile 12 geschaltet sind, aus der Trommel 1 abgelassen werden, wozu das Kolbenventil 12 mit Öffnungswasser beaufschlagt wird, welches durch eine Einspritzkammer 13 für Öffnungswasser und eine Zuleitung 14 zum Kolbenventil 12 geleitet wird. Die Funktion eines solchen Kolbenventils 12 ist im Bereich selbstentleerender Separatoren an sich bekannt.In the
Zum Durchführen einer Entleerung wird Öffnungswasser eingespritzt, welches den Ventilkolben 16 des Kolbenventils 12 verschiebt, so dass das Schließwasser aus der Schließwasseröffnung 15 über die Bohrung 11 und das Ventil 12 ablaufen kann.To perform a drain opening water is injected, which moves the
Je nach Zeitdauer der Öffnungswasserzugabe bzw. je nach Öffnungswassermenge (zugeführt über einen Dosierkolben oder über eine Zeitsteuerung der Öffnung des Zuleitungsventils) entleert die Schließkammer 8 ganz oder teilweise und der Kolbenschieber 5 bewegt sich durch die Druckkraft im Trennraum 3, welche durch das Produkt in der Trommel und die Zentrifugalwirkung erzeugt wird, nach unten und öffnet die Trommel 1.Depending on the duration of the opening water addition or depending on the amount of opening water (supplied via a metering or a timing of the opening of the supply valve) empties the
Öffnungswasser und Schließwasser werden mittels Steuerwasserzuführungen 22a, b durch zwei getrennte Wasserzuleitungen in die Einspritzkammern 13 bzw. 9 in die Trommel gespritzt.Opening water and closing water are sprayed by means of control
Wenn kein Öffnungswasser mehr zugeführt wird, bewegt sich der Ventilkolben nach außen (durch die Zentrifugalkraft) und verschließt die Bohrung 11. Wird die Öffnungskraft schließlich kleiner als die Schließkraft in der Schließkammer 8, in welche Schließwasser eingespritzt wird, bewegt sich der Kolbenschieber 5 wieder aufwärts, was die Trommel 1 verschließt.When no more opening water is supplied, the valve piston moves outward (by the centrifugal force) and closes the
Erfindungsgemäß wird die Schließkammerhöhe, d.h der Abstand zwischen der Trommelinnenwand und dem Kolbenschieber im Bereich der Schließkammer 8, relativ gering gehalten, vorzugsweise beträgt die Höhe 0,3 mm bis 5mm, insbesondere 0,5 bis 1,5 mm.According to the invention, the closing chamber height, that is to say the distance between the inner wall of the drum and the spool in the region of the
Hierdurch wird auch das Schließwasservolumen gering gehalten. Die Höhe der Kammer beeinflusst die Geschwindigkeit der Entleerung signifikant.As a result, the volume of closed water is kept low. The height of the chamber significantly affects the rate of evacuation.
Um dennoch einen relativ großen Entleerungshub zu erhalten und um zu einem schnellen Öffnungsvorgang zu Beginn der Entleerung und zu einem schnellen Schließvorgang gegen Ende der Entleerung zu gelangen, wird dabei aber ein definierter Stufensprung der Schließkammer 8 auf einem vorgegebenen Durchmesser der Schließkammer festgelegt. Im Bereich dieses Stufensprunges vervielfacht sich vorzugsweise die Höhe der Schließkammer 8, vorzugsweise beträgt die Höhe der Schließkammer 8 im Bereich der Ausnehmungen 17 nach Versuchen das drei- bis fünfzehnfache der Spalthöhe der Schließkammer 8 im Bereich neben bzw. außerhalb der Ausnehmungen 17, insbesondere 3 bis 20 mm, besonders vorteilhaft 5 bis 12 mm, insbesondere 10 mm.In order nevertheless to obtain a relatively large discharge stroke and to arrive at a rapid opening operation at the beginning of the emptying and a fast closing operation towards the end of emptying, but a defined increment of the
Vorzugsweise wird dieser Stufensprung im Bereich des unteren Teiles des Kolbenschiebers eingebracht. Dieser Umkehrbereich des Winkels des Kolbenschiebers liegt in der Regel - vom Außendurchmesser des Kolbenschiebers aus betrachtet - zwischen einem Drittel und zwei Drittel seines Radius.Preferably, this increment is introduced in the region of the lower part of the piston slide. This reversal range of the angle of the spool is usually - viewed from the outside diameter of the spool - between one third and two thirds of its radius.
Zusätzlich weist der Kolbenschieber hier an seiner Unterseite in seinem inneren und äußeren Randbereich Umfangsfreidrehungen 20, 21 zur besseren Annahme und zum besseren Abfuhr des Schließwassers auf.In addition, the spool has here on its underside in its inner and outer edge region circumferential
Die Erfindung lässt sich beispielsweise auf einfache Weise dadurch realisieren, dass in die der Schließkammer zugewandte Seite des Kolbenschiebers 6 auf einem bestimmten Durchmesser Ausnehmungen 17 eingebracht werden, beispielsweise zwei oder mehr umfangsverteilte Ausfräsungen. Die Ausnehmungen 17 führen zu einem optimierten Entleerungsverhalten, wie es beispielhaft in
Wie aus der
Darüber hinaus ergibt sich durch die Spaltverbreiterung im Bereich der Ausnehmungen 17 - die beispielsweise als Ausfräsungen ausgelegt sein können - ein automatisches und zu Beginn des Schließvorganges sehr schnelles Schließverhalten, bis auf einen geringen Restspalt.In addition, results from the gap widening in the region of the recesses 17 - which may be designed, for example, as recesses - an automatic and at the beginning of the closing process very fast closing behavior, except for a small residual gap.
Durch eine geeignete Auslegung - bzw. Variation - des Schließspaltes und der Ausnehmungen 17 kann somit die Entleerungscharakteristik bzgl. der Entleerungsgeschwindigkeit und der Entleerungsmenge gezielt eingestellt werden.By a suitable design - or variation - of the closing gap and the
Die Ausfräsungen 17 erhöhen zudem die Unempfindlichkeit gegen Ventilsteuerzeitschwankungen, so dass sogar auf einen Dosierkolben, der zur Einstellung und Steuerung von Teilentleerungen dient, verzichtet werden kann, was die Kosten der Konstruktion gegenüber bekannten Lösungen senkt.The
Die Ausfräsungen 17 werden je nach Art der zu verarbeitenden Produktes und der durchzuführenden Entleerungen (Teilentleerungsmenge) ausgelegt, was beispielsweise empirisch mit Hilfe durch Versuche erfolgen kann, bis sich eine Charakteristik nach Art der
Die einmal ermittelte Charakteristik des Öffnungsweges und der Teilentleerungsmenge wird reproduzierbar erreicht. Gewünschte Veränderungen können durch ein Anpassen der Ausnehmung 17 und deren Volumen erreicht werden.Once determined characteristic of the opening path and the Teilentleerungsmenge is achieved reproducibly. Desired changes can be achieved by adjusting the
Der Kolbenschieber der
Es wäre auch denkbar, nur eine Ausfräsung vorzusehen und diese als eine umlaufende Ringnut auszubilden. Aus Stabilitätsgründen und in Hinsicht auf eine besonders optimale Entleerung scharakteristik ist es aber vorteilhaft, zwischen den umfangsverteilten Ausfräsungen 17 auch Bereiche des Kolbenschiebers stehenzulassen, in denen die Wanddicke des Kolbenschiebers nicht durch die eine oder mehreren Ausnehmungen 17 geschwächt ist.It would also be conceivable to provide only one cutout and to form this as a circumferential annular groove. For reasons of stability and in terms of a particularly optimal emptying sharp characteristic, it is advantageous to leave between the circumferentially distributed
Wenn die Ausfräsung(en) 17 im Kolbenschieber weiter außen liegt bzw. liegen, so vergrößert sich die Austragsmenge des Feststoffes bei der Teilentleerung. Liegt die Position weiter innen, verkleinert sich die Austragsmenge bei gleicher Ventilöffnungszeit.If the cutout (s) 17 in the piston valve is located farther out or, so increases the discharge of the solid at the partial emptying. If the position is further inside, the discharge volume decreases with the same valve opening time.
Der Vergleich der Entleerungscharakteristiken, wie er in
- Trommeldrum
- 11
- Schleuderraumcentrifugal chamber
- 22
- Trennraumseparating space
- 33
- FeststoffraumSolid space
- 44
- Kolbenschieberspool
- 55
- Trommelmanteldrum shell
- 66
- Auswurföffnungenejection openings
- 77
- Schließkammerclosing chamber
- 88th
- EinspritzkammerInjection chamber
- 99
- Zuleitungsupply
- 1010
- Ableitungenderivations
- 1111
- Kolbenventilepiston valves
- 1212
- EinspritzkammerInjection chamber
- 1313
- Kanalchannel
- 1414
- SchließwasseröffnungClosing water opening
- 1515
- Ventilkolbenplunger
- 1616
- Ausnehmungrecess
- 1717
- konische Bereicheconical areas
- 18, 1918, 19
- UmfangsfreidrehungenScope of free spins
- 20, 2120, 21
- SteuerwasserzuführungControl water supply
- 22a, b22a, b
Claims (10)
- A centrifuge, comprising a self-emptying centrifuge drum, in the drum shell (6) of which discharge openings (7) are formed, said openings originating from a solids chamber (4) and being closable by way of an axially movable piston slide (5), wherein a closing chamber (8) to which closing fluid can be applied is associated with the piston slide (5), which closing chamber can be discharged by actuating one or several hydraulic valves (12) by means of opening fluid, wherein the closing chamber (8) comprises at least one or several recesses (17), in the region of which the closing chamber (8) has a greater closing chamber height than in the remaining area thereof outside of the recesses (17), wherein the piston slide (5) has a double conical shape radially to the inside and to the outside, characterized in that the recesses are formed as milled-out portions formed in the transitional region between the two conical regions (18 and 19).
- A centrifuge according to claim 1, characterized in that the recesses (17) are formed as cavities in the side of the piston slide (5) which faces the closing chamber (8).
- A centrifuge according to claim 1 or 2, characterized in that the hydraulic valves are formed as piston valves (12).
- A centrifuge according to claim 2, characterized in that the one or several recesses (17) are introduced in a circumferentially distributed manner on a specific diameter into the side of the piston slide (6) facing the closing chamber.
- A centrifuge according to one of the preceding claims 2 or 4, characterized in that the milled-out portions (17) are introduced in a circumferentially distributed manner into the side of the piston slide facing the closing chamber.
- A centrifuge according to one of the preceding claims 1 to 3, characterized in that the at least one recess (17) is formed as a circumferential annular groove.
- A centrifuge according to one of the preceding claims, characterized in that the closing chamber height, i.e. the distance between the inner wall of the drum and the piston slide, amounts to 0.3 to 5 mm in the region of the closing chamber (8).
- A centrifuge according to one of the preceding claims, characterized in that the closing chamber height, i.e. the distance between the inner wall of the drum and the piston slide, amounts to 0.5 to 1.5 mm in the region of the closing chamber (8).
- A centrifuge according to claim 8, characterized in that the closing chamber height, i.e. the distance between the inner wall of the drum and the piston slide, amounts to 3 to 20 mm, especially 5 to 12 mm, in the region of the recesses (8).
- A centrifuge according to one of the preceding claims, characterized in that in the region of the recesses (17) the height of the closing chamber (8) is 3 to 15 times the height of the closing chamber (8) in the region adjacent to the recesses (17).
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE200810048934 DE102008048934A1 (en) | 2008-09-25 | 2008-09-25 | Centrifuge with a self-cleaning centrifugal drum |
PCT/EP2009/062339 WO2010034751A1 (en) | 2008-09-25 | 2009-09-23 | Centrifuge with a self-emptying centrifuge drum |
Publications (2)
Publication Number | Publication Date |
---|---|
EP2326427A1 EP2326427A1 (en) | 2011-06-01 |
EP2326427B1 true EP2326427B1 (en) | 2017-01-11 |
Family
ID=41422648
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP09783343.8A Active EP2326427B1 (en) | 2008-09-25 | 2009-09-23 | Centrifuge having a selfdischarging bowl |
Country Status (4)
Country | Link |
---|---|
EP (1) | EP2326427B1 (en) |
CN (1) | CN102164679B (en) |
DE (1) | DE102008048934A1 (en) |
WO (1) | WO2010034751A1 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2774684B1 (en) * | 2013-03-06 | 2018-10-17 | Alfa Laval Corporate AB | A centrifugal separator |
EP2808086A1 (en) * | 2013-05-27 | 2014-12-03 | Alfa Laval Corporate AB | Centrifugal separator and method for determining suitable moment for removal of heavy phase content |
Family Cites Families (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DK117207B (en) * | 1960-04-20 | 1970-03-23 | Separator Ab | Sludge centrifuge. |
SE321896B (en) | 1968-02-29 | 1970-03-16 | Alfa Laval Ab | |
DE3012108C2 (en) * | 1980-03-28 | 1982-09-23 | Westfalia Separator Ag, 4740 Oelde | Self-emptying centrifugal drum |
DE3208808C2 (en) | 1982-03-11 | 1984-11-22 | Westfalia Separator Ag, 4740 Oelde | Centrifuge with a self-cleaning centrifugal drum |
DE3240093C2 (en) | 1982-10-29 | 1986-03-27 | Westfalia Separator Ag, 4740 Oelde | Centrifuge with a self-cleaning centrifugal drum |
DE3240998C2 (en) * | 1982-11-06 | 1985-05-30 | Westfalia Separator Ag, 4740 Oelde | Centrifuge with a self-cleaning centrifugal drum |
DE3607526A1 (en) | 1985-03-14 | 1987-09-10 | Westfalia Separator Ag | Centrifuge with a self-emptying centrifuge drum |
DE3509139C1 (en) | 1985-03-14 | 1986-04-17 | Westfalia Separator Ag, 4740 Oelde | Centrifuge with a self-draining centrifuge |
DE3524731C1 (en) | 1985-07-11 | 1986-11-27 | Westfalia Separator Ag, 4740 Oelde | Centrifuge with a self-draining centrifuge |
DE4436459C2 (en) * | 1994-10-12 | 1997-04-24 | Flottweg Gmbh | Centrifugal drum |
SE510541C2 (en) * | 1997-09-29 | 1999-05-31 | Alfa Laval Ab | Centrifugal separator control device |
SE529562C2 (en) * | 2006-02-13 | 2007-09-18 | Alfa Laval Corp Ab | Ways of monitoring centrifugal separator |
-
2008
- 2008-09-25 DE DE200810048934 patent/DE102008048934A1/en not_active Withdrawn
-
2009
- 2009-09-23 CN CN200980137322.8A patent/CN102164679B/en active Active
- 2009-09-23 EP EP09783343.8A patent/EP2326427B1/en active Active
- 2009-09-23 WO PCT/EP2009/062339 patent/WO2010034751A1/en active Application Filing
Non-Patent Citations (1)
Title |
---|
None * |
Also Published As
Publication number | Publication date |
---|---|
WO2010034751A1 (en) | 2010-04-01 |
EP2326427A1 (en) | 2011-06-01 |
CN102164679B (en) | 2016-03-30 |
DE102008048934A1 (en) | 2010-04-01 |
CN102164679A (en) | 2011-08-24 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0702599B1 (en) | Weir for a solid-jacket centrifuge drum | |
EP2902112B1 (en) | Outlet device of a solid bowl screw centrifuge | |
EP2658656B1 (en) | Solid bowl screw centrifuge having an overflow weir | |
EP2451585B1 (en) | Separator comprising a vertical rotational axis | |
EP4168223A1 (en) | Nozzle for dispensing concrete, mortar or the like | |
WO2003064054A1 (en) | Full-jacket helix centrifuge with a weir | |
EP1732697B9 (en) | Solid-wall centrifuge comprising a weir provided with a stationary deflector plate | |
DE10334032B4 (en) | valve means | |
DE10209925B4 (en) | Three-phase solid bowl screw centrifuge, solid bowl screw centrifuge and method of operating a three-phase solid bowl screw centrifuge | |
DE202016101272U1 (en) | separator | |
EP2928613B1 (en) | Outlet nozzle for a centrifuge drum | |
EP2326427B1 (en) | Centrifuge having a selfdischarging bowl | |
EP2913112A1 (en) | Centrifuge, and method for loading a centrifuge | |
EP3328550A1 (en) | Separator drum and separator | |
EP1998896B1 (en) | Fully jacketed screw centrifuge with efflux orifices for partial and residual emptying of the drum | |
EP0332868B1 (en) | Rotating or sliding gate valve for an outlet of vessels containing molten metal | |
EP2551019B1 (en) | Solid bowl screw centrifuge with a weir edge | |
DE2852628A1 (en) | SEPARATOR | |
EP2026909B1 (en) | Centrifuge, in particular separator, having a feed line for control fluid | |
EP3720611B1 (en) | Separator drum | |
EP1949966B1 (en) | Solid wall helical centrifuge with pressure plate | |
DE3119423C1 (en) | Self-draining centrifugal drum | |
EP0531606A1 (en) | Flow control valve | |
DE3141356A1 (en) | Centrifuge with volumetrically metered discharge of the denser component | |
DE3829158A1 (en) | Self-emptying drum separator |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
17P | Request for examination filed |
Effective date: 20110222 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO SE SI SK SM TR |
|
AX | Request for extension of the european patent |
Extension state: AL BA RS |
|
DAX | Request for extension of the european patent (deleted) | ||
GRAP | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOSNIGR1 |
|
INTG | Intention to grant announced |
Effective date: 20160801 |
|
GRAS | Grant fee paid |
Free format text: ORIGINAL CODE: EPIDOSNIGR3 |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO SE SI SK SM TR |
|
REG | Reference to a national code |
Ref country code: GB Ref legal event code: FG4D Free format text: NOT ENGLISH |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: EP |
|
REG | Reference to a national code |
Ref country code: AT Ref legal event code: REF Ref document number: 860770 Country of ref document: AT Kind code of ref document: T Effective date: 20170115 |
|
REG | Reference to a national code |
Ref country code: IE Ref legal event code: FG4D Free format text: LANGUAGE OF EP DOCUMENT: GERMAN |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R096 Ref document number: 502009013568 Country of ref document: DE |
|
REG | Reference to a national code |
Ref country code: SE Ref legal event code: TRGR |
|
REG | Reference to a national code |
Ref country code: LT Ref legal event code: MG4D |
|
REG | Reference to a national code |
Ref country code: NL Ref legal event code: MP Effective date: 20170111 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: NL Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20170111 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: FI Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20170111 Ref country code: NO Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20170411 Ref country code: LT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20170111 Ref country code: HR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20170111 Ref country code: GR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20170412 Ref country code: IS Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20170511 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: PL Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20170111 Ref country code: PT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20170511 Ref country code: ES Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20170111 Ref country code: BG Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20170411 Ref country code: LV Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20170111 |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R097 Ref document number: 502009013568 Country of ref document: DE |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20170111 Ref country code: EE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20170111 Ref country code: CZ Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20170111 Ref country code: RO Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20170111 Ref country code: IT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20170111 |
|
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SM Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20170111 Ref country code: DK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20170111 |
|
26N | No opposition filed |
Effective date: 20171012 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SI Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20170111 |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: PL |
|
GBPC | Gb: european patent ceased through non-payment of renewal fee |
Effective date: 20170923 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: MC Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20170111 |
|
REG | Reference to a national code |
Ref country code: IE Ref legal event code: MM4A |
|
REG | Reference to a national code |
Ref country code: BE Ref legal event code: MM Effective date: 20170930 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LU Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20170923 |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: ST Effective date: 20180531 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20170923 Ref country code: GB Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20170923 Ref country code: CH Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20170930 Ref country code: LI Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20170930 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: BE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20170930 Ref country code: FR Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20171002 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: MT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20170111 |
|
REG | Reference to a national code |
Ref country code: AT Ref legal event code: MM01 Ref document number: 860770 Country of ref document: AT Kind code of ref document: T Effective date: 20170923 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: AT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20170923 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: HU Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT; INVALID AB INITIO Effective date: 20090923 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: CY Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20170111 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: MK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20170111 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: TR Payment date: 20220920 Year of fee payment: 14 Ref country code: SE Payment date: 20220924 Year of fee payment: 14 |
|
P01 | Opt-out of the competence of the unified patent court (upc) registered |
Effective date: 20230330 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 20230928 Year of fee payment: 15 |
|
REG | Reference to a national code |
Ref country code: SE Ref legal event code: EUG |