EP2326427B1 - Centrifuge having a selfdischarging bowl - Google Patents

Centrifuge having a selfdischarging bowl Download PDF

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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
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EP
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Prior art keywords
closing chamber
recesses
closing
drum
piston slide
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EP09783343.8A
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German (de)
French (fr)
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EP2326427A1 (en
Inventor
Wilfried Mackel
Helga Tietz
Bernd Terwey
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GEA Mechanical Equipment GmbH
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GEA Mechanical Equipment GmbH
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04BCENTRIFUGES
    • B04B1/00Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
    • B04B1/10Centrifuges 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
    • B04B1/14Centrifuges 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04BCENTRIFUGES
    • B04B1/00Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
    • B04B1/10Centrifuges 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
    • B04B1/14Centrifuges 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
    • B04B1/16Centrifuges 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
    • B04B1/18Centrifuges 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.

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  • 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 DE-OS 19 09 996 bekannt. Weiterentwickelte Konstruktionen zeigen die DE 32 08 808 A1 , die DE 32 40 093 A1 , die DE 35 09 139 C1 , die DE 35 24 731 C1 und die DE 36 07 526 A1 . Mit den bekannten - unter dem Namen Hydrostop bekannten - Lösungen lassen sich zwar insbesondere Teilentleerungen präzise steuern, es handelt sich aber um jeweils relativ aufwändige Konstruktionen.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.

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 DE 30 12 108 A1 und die EP 0 706 829 , beide gemäß dem Oberbegriff des Anspruchs 1. genannt.The state of the art in addition to its DE 30 12 108 A1 and the EP 0 706 829 Both named according to the preamble of claim 1.

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.
The invention will be described in more detail with reference to the drawing. Show it:
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 Fig. 4) einer drehbaren Trommel 1 eines (Teller-)Separators mit vertikaler Drehachse zugeführt, die einen Schleuderraum 2 aufweist, der sich in einen Trennraum 3 und einen Feststoffraum 4 unterteilt.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.

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 movable piston slide 5, which releases or closes during its axial movements in the drum shell 6 ejection openings 7 for the solids.

Zwischen dem Kolbenschieber 5 und dem Trommelmantel 6 bzw. dem Trommelunterteil ist eine mit Schließfluid beaufschlagbare Schließkammer 8 ausgebildet.Between the piston slide 5 and the drum shell 6 and the drum base is acted upon with a closing fluid lock chamber 8 is formed.

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 closing chamber 8 10 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.

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 valve piston 16 of the spool valve 12, so that the closing water from the closing water opening 15 via the bore 11 and the valve 12 can drain.

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 closing chamber 8 wholly or partially and the spool 5 moves through the pressure force in the separation chamber 3, which by the product in the Drum and the centrifugal action is generated, down and opens the drum. 1

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 water supply lines 22a, b through two separate water supply lines into the injection chambers 13 and 9, respectively, into the drum.

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 bore 11. When the opening force is finally smaller than the closing force in the closing chamber 8, in which closing water is injected, the spool 5 moves up again , which closes the drum 1.

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 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.

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 lock chamber 8 is set to a predetermined diameter of the lock chamber. Preferably, 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.

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 free rotations 20, 21 for better acceptance and for better removal of the closing water.

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 Fig. 2 abgebildet ist.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.

Wie aus der Fig. 2 ersichtlich, ergibt sich durch den schmalen Spaltraum im inneren radialen Bereich der Schließkammer 8 bei der gewählten beispielhaften Auslegung für eine Trommel 1, die einen Böschungswinkel α von 15° aufweist, zu Beginn der Entleerung ein deutlich vergrößerter Entleerungshub und ein schneller Öffnungsvorgang.Like from the Fig. 2 can be seen results from the narrow gap in the inner radial region of the lock chamber 8 in the selected exemplary design for a drum 1, which has a slope angle α of 15 °, at the beginning of the emptying a significantly increased discharge stroke and a faster opening operation.

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 recesses 17 thus the emptying characteristic with respect. The emptying speed and the emptying amount can be adjusted specifically.

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 recesses 17 also increase the insensitivity to valve timing variations, so that even a metering piston, which serves to adjust and control of partial discharges, can be dispensed with, which reduces the cost of construction over known solutions.

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 Fig. 2 mit einem relativ großen, schnell auf einen maximalen Wert ansteigenden Öffnungshub und einem relativ schnellen Stoppen der Entleerung ergibt.The cutouts 17 are designed depending on the nature of the product to be processed and the emptying (Teilentleerungsmenge) 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.

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 recess 17 and its volume.

Der Kolbenschieber der Fig. 1 weist ausgehend von einem Radius R17 im Bereich der Ausfräsungen radial nach innen und nach außen hin doppelt konische Form auf, wobei die Ausfräsungen 17 im Übergangsbereich 17 zwischen den beiden konischen Bereichen 18 und 19 beispielhaft als zwei Varianten ausgebildet sind.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.

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 cutouts 17 and areas of the piston valve, in which the wall thickness of the piston valve is not weakened by the one or more recesses 17.

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 Fig. 2 und 3 dargestellt ist, wurde beispielhaft mit einem Separator vom Typ MSD 300 der Anmelderin durchgeführt. Die Hubhöhe von 100% bezieht sich auf die mechanisch realisierbare Bewegungsmöglichkeit des Kolbenschiebers zwischen dem Trommeldeckel und dem Trommelunterteil. Die Zeitbasis von beispielsweise 1 sec bezieht sich auf die Ansteuerung des vorgeschalteten Magnetventils zur Zuführung des Öffnungswassers.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.

Bezugszeichenreference numeral

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)

  1. 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).
  2. 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).
  3. A centrifuge according to claim 1 or 2, characterized in that the hydraulic valves are formed as piston valves (12).
  4. 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.
  5. 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.
  6. 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.
  7. 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).
  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).
  9. 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).
  10. 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).
EP09783343.8A 2008-09-25 2009-09-23 Centrifuge having a selfdischarging bowl Active EP2326427B1 (en)

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)

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* Cited by examiner, † Cited by third party
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

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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

Non-Patent Citations (1)

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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

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