DK2551019T3 - Full cloak-Solid-bowl screw spillway - Google Patents

Full cloak-Solid-bowl screw spillway Download PDF

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Publication number
DK2551019T3
DK2551019T3 DK11006261.9T DK11006261T DK2551019T3 DK 2551019 T3 DK2551019 T3 DK 2551019T3 DK 11006261 T DK11006261 T DK 11006261T DK 2551019 T3 DK2551019 T3 DK 2551019T3
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DK
Denmark
Prior art keywords
outlet channel
full
centrifuge
centrifuge drum
drum
Prior art date
Application number
DK11006261.9T
Other languages
Danish (da)
Other versions
DK2551019T4 (en
Inventor
Manfred Schlarb
Benno Vielhuber
Wieland Zaglauer
Original Assignee
Flottweg Se
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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
    • B04B1/20—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles discharging solid particles from the bowl by a conveying screw coaxial with the bowl axis and rotating relatively to the bowl
    • 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
    • B04B1/20—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles discharging solid particles from the bowl by a conveying screw coaxial with the bowl axis and rotating relatively to the bowl
    • B04B2001/2075—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles discharging solid particles from the bowl by a conveying screw coaxial with the bowl axis and rotating relatively to the bowl with means for recovering the energy of the outflowing liquid
    • 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
    • B04B1/20—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles discharging solid particles from the bowl by a conveying screw coaxial with the bowl axis and rotating relatively to the bowl
    • B04B2001/2083—Configuration of liquid outlets

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  • Centrifugal Separators (AREA)

Description

Background of the invention
The invention relates to a solid bowl screw centrifuge having a centrifuge drum rotatable about a longitudinal axis, which comprises at least one outlet opening for discharging clarified material from the centrifuge drum via a weir edge to be flowed over by the outflowing material and an outlet channel for conveying all of the discharged material, wherein the weir edge is arranged at the front side of the centrifuge drum and the outlet channel extends in the direction of flow downstream of the weir edge, the outlet channel has a curved design in order to divert the outflowing material in a substantially tangential direction, and the outlet channel has a bottom surface, which at least partially is largely of flat design. Such a solid bowl screw centrifuge is also described in particular in WO 2012 089492 A1 which was published subsequently.
Drive energy is known to be required to rotate the centrifuge drum of such a solid bowl screw centrifuge because kinetic energy is transferred to the material to be clarified or centrifuged when said material is introduced. Conversely, the kinetic energy of the clarified outflowing material is converted into friction energy when the drum is emptied.
Efforts are known which use the kinetic energy of the outflowing material wherever possible such that said outflowing material contributes again to driving the rotational movement of the centrifuge drum. Outlet channels in the form of pipes on outlet openings on the front side of the centrifuge drum are known inter alia for this purpose, which divert the flow of material in a tangential direction. The material then exiting not in an axial direction, but in a tangential direction, supplies the centrifuge drum with an impulse in the direction of rotation on account of its centrifugal force which drives the centrifuge drum in the direction of rotation. Such outlet channels are known, for example, from DE 31 12 585 A1, US 2004/0072668 A1 and US 2004/0072667 A1. A solid bowl centrifuge is known from JP 11 197547 A in which a deflector plate is provided which deflects the outflowing material from the axial direction of flow radially outwards. The deflector plate is open radially to the outside. A solid bowl centrifuge with wing plates is known from JP 11 179236 A, which are struck by outflowing material in flight.
Underlying task
The invention is based on the task of creating a solid bowl screw centrifuge in which energy recovery can be provided particularly cost-effectively and at the same time particularly effectively based on impulse feedback from the outflowing material.
Solution according to the invention
This object is achieved according to the invention with a solid bowl screw centrifuge having a centrifuge drum rotatable about a longitudinal axis, which comprises at least one outlet opening for discharging clarified material from the centrifuge drum via a weir edge to be flowed over by the outflowing material and an outlet channel for conveying all of the discharged material, wherein the weir edge is arranged at the front side of the centrifuge drum and the outlet channel extends in particular outwards, in the direction of flow downstream of the weir edge, the outlet channel has a curved design in order to divert the outflowing material in a substantially tangential direction, and the outlet channel has a bottom surface, which at least partially is largely of flat design, wherein the largely flat portion of the bottom surface is inclined radially inwards at an angle of 8° to 28° to the tangential direction.
The discharge device according to the invention is provided at the front side of the centrifuge drum for discharging clarified material from a centrifuge drum and an associated outlet opening is added there partially overlapping in a fixed or adjustable manner. The discharge device comprises a weir with a weir edge and an outlet channel arranged outside upstream of the weir for conveying all of the discharged material. The then axially outflowing material flows through the outlet opening and out over the weir edge aligned there in a radial direction, i.e. transversely to the longitudinal axis. The weir edge has an in particular curved design here and is spaced at a distance of a first radius from the longitudinal axis. The outlet channel following in the direction of flow has a curved design in order to divert the outflowing material in a substantially tangential direction. The outlet channel is designed with a bottom surface over which the material flows. Said bottom surface is spaced at a further distance from the longitudinal axis than the first radius measures, preferably at least in sections.
In the solid bowl screw centrifuge according to the invention, a weir is provided at the front side, which, as in the case in conventional weirs, has its weir edge in the radial plane of the front side. The weir arranged in this manner leads to particularly precise control of the material level inside the centrifuge drum. Moreover, such a weir only has a slight propensity to clog and is also extremely cost-effective to produce. It can be provided with a weir edge designed to be particularly wear-resistant in the style of conventional weirs. Furthermore, it can be well maintained and replaced. The device according to the invention can therefore be used in existing systems as a particularly good alternative. The outlet channel is configured on the outside of the weir. The bottom surface of said channel lies radially further to the outside than the weir edge, preferably at least in sections. This produces a flow that is at least slightly oriented in an external, radial direction downstream of the radially aligned weir edge according to the invention on account of the centrifugal force acting on the material, which leads to eddying at the weir edge and a slightly higher speed of flow there. This type of flow at the weir edge has proven particularly advantageous in terms of controlled discharge of the material and also in terms of potential clogging.
After the stream of outflowing material has flowed over the weir edge by means of the outlet channel according to the invention, said stream is diverted such that its movement impulse essentially oriented in an external radial direction due to centrifugal force is turned in a tangential direction and thus in a direction that drives the centrifuge drum. The outlet channel according to the invention thus achieves two effects. It enables a controlled flow over the weir edge in a radial direction with only slight turbulence, low risk of imbalance and low risk of clogging. At the same time, the outlet channel leads the outflowing material in the required direction in a targeted manner in order to recover a significant amount of energy from the outflowing material.
The bottom surface of the outlet channel of this type is at least partially designed as flat or largely flat. Such a bottom surface can be manufactured at low-cost. Moreover, the material flowing out over it experiences uniform acceleration over a longer distance which can be easily verified using technical models. This acceleration leads to increased conversion of the centrifugal force impulse into a movement impulse in a tangential direction. A particularly large percentage of the centrifugal force energy is converted into tangential drive energy.
The flat or largely flat portion of the bottom surface is inclined radially inwards at an angle of 8° to 28°, preferably 18°, to the tangential direction. Such orientation of the diverted jet of material leads to a specifically targeted deceleration of the exiting stream compared with a purely tangential flow and thus to a certain blockage effect. Such blocking increases the potential energy and thus improves subsequent conversion into tangential kinetic energy.
In a particularly preferred embodiment, the bottom of the outlet channel according to the invention is designed such that its flat or largely flat portion starts from the centre of the outlet opening at an angle of 3.5° counter to the direction of rotation of the centrifuge drum. Such a flat or largely flat portion does not start at the outlet opening until a predefined distance downstream of the centre of the outlet opening. The acceleration of the exiting material achieved there according to the invention therefore does not start until further downstream in the outlet channel. The eddying produced as a result of the acceleration therefore also occurs comparatively further downstream in the outlet channel, whereby there is an overall increase in speed in the outlet channel which sucks the material out. This eddying effect reduces the risk of clogging and at the same time increases the kinetic energy in a tangential direction.
Viewed from the centre of the outlet opening, the flat or largely flat portion of the bottom surface ends particularly preferably counter to the direction of rotation of the centrifuge drum after an angle of 15° to 30°, preferably 21.5°. Such a flat or largely flat portion has a particularly advantageous length, which has proven extremely effective even in the case of different outlet diameters and drum sizes.
In a further particularly advantageous embodiment of the solution according to the invention, a curved portion, in particular a circular arc-shaped curved portion, of the bottom surface adjoins the flat or largely flat portion of the bottom surface, viewed in the direction of rotation of the centrifuge drum. Such a curved portion can be manufactured at low-cost and over a certain range of angles leads to a radially unchanged, and thus radially also unaccelerated or decelerated flow. Such a flow has proven particularly advantageous over a certain portion in the circumferential direction. Particularly advantageous is said curved, radially constant bottom surface, viewed counter to the direction of rotation over the first circumferential portion of the respective outlet opening. Said bottom surface leads to a largely turbulence-free flow at the weir edge and thus to less imbalance development at the plurality of weirs distributed over the circumference of the centrifuge drum over which outflowing material flows.
The outlet channel of curved design according to the invention preferably has a first width, viewed in the longitudinal direction of the centrifuge drum, and a second width, viewed in the radial direction, wherein the second width is designed smaller than the first width. The outlet channel therefore tapers proceeding from the outlet openings in the direction of flow to the end of the outlet channel at which the outflowing material is released largely in a tangential direction. This tapering brings about a constant increase in the speed of the material flow and thus the kinetic energy of the outflowing material.
It is therefore particularly advantageous if the curved outlet channel viewed in the discharge direction is designed as continuously tapering in terms of its width. Acceleration then occurs largely turbulence-free with simultaneous specifically directed flow through the outlet openings and the subsequent outlet channels.
An outlet channel of this type is preferably designed radially inwardly open. The outlet channel is therefore unlike solutions known from the prior art where the outflowing material is diverted through one or more pipes in a tangential direction.
The radially inwardly open channel according to the invention cannot only be manufactured at low cost, but overall has less risk of clogging. Furthermore, such a channel can be cleaned more easily during maintenance work as it is more accessible.
The weir edge and the outlet channel of the solid bowl screw centrifuge according to the invention are preferably designed with a component or as one piece or integrally, wherein the component can be advantageously attached, in particular from the outside, to the front side of the centrifuge drum and detached therefrom. The component can then be retrofitted easily depending on the intended use and can also be easily replaced during maintenance. Furthermore, the position of the weir edge can be easily adjusted. Adjusting the weir edge also changes the position of the associated outlet channel in an advantageous manner without requiring further time-consuming adjustment or alignment work.
Brief description of the drawings
One embodiment of the solution according to the invention is explained in detail below using the attached schematic drawings.
Fig. 1 shows a view of the front side of a centrifuge drum of a solid bowl screw centrifuge with a discharge device arranged thereon for discharging material from the centrifuge drum,
Fig. 2 shows an enlarged view of the discharge device according to Fig. 1,
Fig. 3 shows a side view of the discharge device according to Fig. 2 and Fig. 4 shows a top view of the discharge device according to Fig. 2.
Detailed description of the embodiment
Fig.1 shows the front side of a centrifuge drum 10, which has a centrifuge screw inside (not shown) in accordance with a conventional design of a solid bowl screw centrifuge.
The centrifuge drum 10 is rotatable in a direction of rotation 14 about a longitudinal axis 12 at a high number of revolutions per minute.
Six circular outlet openings 16 are arranged on the front side of the centrifuge drum 10 in a circle at regular intervals about the longitudinal axis 12. The outlet openings 16 serve to convey or discharge clarified (not shown) material from the centrifuge drum 10. A discharge device 18 is attached upstream of each outlet opening 16 externally on the front side of the centrifuge drum 10. Each discharge device 18 is formed as an integral component from a weir plate 20 and an outlet channel 22. The individual weir plate 20 extends in a radial direction, i.e. transversely to the longitudinal axis 12 and is fixedly attached to the front side by means of two screws 24 and is fairly adjustable in terms of its position. A weir edge 26 is configured on each weir plate 20, which is of curved design and spaced at a radius 28 from the longitudinal axis 12. The outflowing material has to flow over said weir edge 26, whereby the level of material in the centrifuge drum 10 can be specifically adjusted depending on the clarification performance required.
The associated outlet channel 22 is arranged externally on each of the weir plates 20 in a longitudinal direction or in the direction of flow over the weir edge 26. Said outlet channel 22 has been manufactured such that it is integrated with the weir plate 20 by means of a milling operation.
The outlet channel 22 receives all the material flowing over the weir edge 26 and thus serves to discharge all of the material discharged from the respective outlet opening 16.
The outlet channel 22 following the weir edge in the direction of flow is substantially rectangular in shape in cross-section and has a bottom surface 30. The bottom surface comprises a curved portion 32, which begins along the weir edge 20 (i.e. in a circumferential direction) viewed counter to the direction of rotation 14 at the start of the outlet opening 16 and ends after an angle 34 of 3.5° upstream of the centre of the outlet opening 16. The curved portion 32 is of curved design as per the curved surface area of a circular cylinder with the radius 28. A flat portion 36 of the bottom surface 30 adjoins the curved portion 32 viewed counter to the direction of rotation 14. Said portion 36 extends proceeding from the angle 34 to an angle 38 of 21.6°. The flat portion 36 is inclined radially inwards at an angle 40 of 18° to the tangential direction. The flat portion 36 is therefore spaced further away from the longitudinal axis 12 than the radius 28 measures. The material flowing out over the flat portion 36 experiences uniform acceleration over a longer distance which can be easily verified using technical models. This acceleration leads to increased conversion of the centrifugal force impulse into a movement impulse in a tangential direction. Since, in particular the entire quantity of material flows through the outlet channel 22, a particularly large percentage of the centrifugal force energy from the outflowing material is converted into tangential drive energy for the rotational movement of the centrifuge drum 10.
Said acceleration effect in the outlet channel 22 is supported by a continuous tapering of the outlet channel 22 in the direction of flow of the material, i.e. in a tangential direction. Said tapering is formed in that the outlet channel 22 proceeding from a first width 42 for the inflowing material, i.e. viewed in a longitudinal direction, tapers to a second width 44 for the outflowing material, i.e. viewed in a tangential or radial direction. The widths 42 and 44 are defined by two side walls 46 and 48 of the outlet channel 22, which, proceeding from the longitudinal direction, are curved accordingly in the tangential direction.
At the same time, an outlet channel 22 of this type is designed with a radially inwardly completely open region 50. Said region 50 allows free adjustment of the material level in the outlet channel 22. Since the material can therefore flow away freely through the outlet channel 22, there can be no clogging and the material level can be freely adjusted at the associated weir edge 26 depending on the level of material in the centrifuge drum 10.
Not least, particularly precise control of the material level inside the centrifuge drum 10 is possible using the weir plates 20 and the weir edges 26 radially aligned there, even if the operating conditions fluctuate significantly.
Once the material has flowed over the radially aligned weir edge 26, the material flows are diverted such that on account of their flow through the outlet channel 22 they have a movement impulse rotated radially inwards from the tangential direction in the region of 8° to 28°, preferably 18°. The movement impulse aligned in this manner has proven particularly advantageous in terms of the energy recovery back into the centrifuge drum 10 that is produced.
List of reference numerals 10 Centrifuge drum 12 Longitudinal axis 14 Direction of rotation 16 Outlet openings 18 Discharge device as integral component 20 Weir plate 22 Outlet channel 24 Screw 26 Weir edge 28 Radius 30 Bottom surface 32 Curved portion of bottom surface 34 Angle (3.5°) 36 Flat portion of bottom surface 38 Angle (21.6°) 40 Angle (18.0°) 42 First width (viewed in longitudinal direction) 44 Second width (viewed in radial direction) 46 Side wall 48 Side wall 50 Radially inwardly open region

Claims (10)

1. Fuldkappe-snekkecentrifuge der har en centrifugetromle (10), der er rotérbar rundt om en længdeakse, som omfatter mindst en udløbsåbning (16) til udtømning af renset materiale fra centrifugetromlen (10) via en overløbskant (26) som overløbes af det udflydende materiale og en udløbskanal (22) til bortledning af hele det udledte materiale, hvor overløbskanten (26) er anbragt på fronten af centrifugetromlen (10) og udløbskanalen (22) udstrækker sig i strømningsretning bag overløbskanten (26), udløbskanalen (22) er buet i konstruktion for at bortlede det udflydende materiale i en i det væsentlige tangential retning, og udløbskanalen (22) har en bundoverflade (30) som i det mindste delvist overvejende er flad i konstruktion, kendetegnet ved at, den overvejende flade del (36) af bundoverfladen (30) er skrånende radialt indad i en vinkel på 8° til 28° i forhold til den tangentiale retning.A full-cap worm centrifuge having a centrifuge drum (10) rotatable about a longitudinal axis comprising at least one outlet opening (16) for discharging cleaned material from the centrifuge drum (10) via an overflow edge (26) which is overflowed by the liquid. material and an outlet channel (22) for draining out all the discharged material, the overflow edge (26) being arranged on the front of the centrifuge drum (10) and the outlet channel (22) extending in flow direction behind the overflow edge (26), the outlet channel (22) being curved in construction to deflect the flowing material in a substantially tangential direction, and the outlet channel (22) has a bottom surface (30) which is at least partially flat in construction, characterized in that the predominantly flat portion (36) of the bottom surface (30) is inclined radially inwardly at an angle of 8 ° to 28 ° relative to the tangential direction. 2. Fuldkappe-snekkecentrifuge ifølge krav 1, hvor bundoverfladens (30) overvejende flade del (36) er skrånende radialt indad i en vinkel på 18° i forhold til den tangentiale retning.The full casing worm centrifuge according to claim 1, wherein the predominantly flat portion (36) of the bottom surface (30) is inclined radially inwardly at an angle of 18 ° to the tangential direction. 3. Fuldkappe-snekkecentrifuge ifølge krav 1 eller 2, hvor bundoverfladens (30) overvejende flade del (36) begynder efter en vinkel på 3,5° fra udløbsåbningens centrum, set modsat centrifugetromlens (10) rotationsretning (14).A full-cap worm centrifuge according to claim 1 or 2, wherein the predominantly flat portion (36) of the bottom surface (30) begins at an angle of 3.5 ° from the center of the outlet opening, as opposed to the direction of rotation (14) of the centrifuge drum (10). 4. Fuldkappe-snekkecentrifuge ifølge et af kravene 1 til 3, hvor bundoverfladens (30) overvejende flade del (36) slutter efter en vinkel på fra 15° til 30°, fortrinsvis 21,5°, fra udløbsåbningens centrum, set modsat centrifugetromlens (10) rotationsretning (14).The full-cap worm centrifuge according to one of claims 1 to 3, wherein the predominantly flat portion (36) of the bottom surface (30) ends at an angle of from 15 ° to 30 °, preferably 21.5 °, from the center of the outlet opening, as opposed to the centrifuge drum ( 10) direction of rotation (14). 5. Fuldkappe-snekkecentrifuge ifølge krav 4, hvor en buet del (32), i særdeleshed en cirkulær-hvælvingsformet buet del af bundoverfladen (30) støder op til bundoverfladens (30) overvejende flade del (36), set i centrifugetromlens (10) rotationsretning (14).The full-cap worm centrifuge according to claim 4, wherein a curved portion (32), in particular a circular-vaulted curved portion of the bottom surface (30) abuts the predominantly flat portion (36) of the bottom surface (30), seen in the centrifuge drum (10). direction of rotation (14). 6. Fuldkappe-snekkecentrifuge ifølge et af kravene 1 til 5, hvor udløbskanalen (22), der har en buet konstruktion, har en første bredde (42) til det indstrømmende materiale, set i centrifugetromlens (10) længderetning, og en anden bredde (44) til det udstrømmende materiale, set i den radiale retning, og hvor den anden bredde (44) er konstrueret mindre end den første bredde (42).The full-cap worm centrifuge according to one of claims 1 to 5, wherein the outlet channel (22) having a curved construction has a first width (42) for the flowing material, seen in the longitudinal direction of the centrifuge drum (10), and a second width ( 44) for the flowing material, viewed in the radial direction, and wherein the second width (44) is constructed less than the first width (42). 7. Fuldkappe-snekkecentrifuge ifølge krav 6, hvor udløbskanalen (22), der har buet konstruktion, har en konstruktion der mindskes kontinuerligt med hensyn til dens bredde, set i udledningsretningen.The full casing worm centrifuge according to claim 6, wherein the curved outlet channel (22) has a construction which is continuously reduced with respect to its width, seen in the discharge direction. 8. Fuldkappe-snekkecentrifuge ifølge et af kravene 1 til 7, hvor udløbskanalen (22) er konstrueret radialt åben indadtil.The full sheath worm centrifuge according to one of claims 1 to 7, wherein the outlet channel (22) is constructed radially open inwardly. 9.9th Fuldkappe-snekkecentrifuge ifølge et af kravene 1 til 8, hvor overløbskanten (26) og udløbskanalen (22) er konstrueret med en komponent (18) som, i særdeleshed fra ydersiden, er fast forbindelig til centrifugetromlens front (10) og aftagelig derfra.Full cover worm centrifuge according to one of claims 1 to 8, wherein the overflow edge (26) and the outlet channel (22) are constructed with a component (18) which, in particular from the outside, is firmly connected to the front (10) of the centrifuge drum and removable therefrom.
DK11006261.9T 2011-07-29 2011-07-29 Full casing worm centrifuge with an overflow edge DK2551019T4 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP11006261.9A EP2551019B2 (en) 2011-07-29 2011-07-29 Solid bowl screw centrifuge with a weir edge

Publications (2)

Publication Number Publication Date
DK2551019T3 true DK2551019T3 (en) 2016-12-12
DK2551019T4 DK2551019T4 (en) 2020-02-03

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ID=45044247

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DK13178930.7T DK2659985T4 (en) 2011-07-29 2011-07-29 Full casing worm centrifuge with overflow edge
DK11006261.9T DK2551019T4 (en) 2011-07-29 2011-07-29 Full casing worm centrifuge with an overflow edge

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DK13178930.7T DK2659985T4 (en) 2011-07-29 2011-07-29 Full casing worm centrifuge with overflow edge

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Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8845506B2 (en) * 2008-08-15 2014-09-30 M-I L.L.C. Centrifuge and changeable weir inserts therefor
DK2789395T4 (en) 2013-04-08 2020-02-10 Flottweg Se Decanter centrifuge with an energy recovery unit
DE102014108722A1 (en) 2014-04-30 2015-11-05 Hiller Gmbh screw centrifuge

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3112585A1 (en) 1981-03-30 1982-10-14 Buckau-Walther AG, 4048 Grevenbroich Method and device for separating a mixture of two materials
JP3543597B2 (en) 1997-12-22 2004-07-14 株式会社クボタ Separation water discharge device in horizontal centrifuge
JPH11197547A (en) † 1998-01-13 1999-07-27 Kubota Corp Device of discharging separated water in a horizontal type centrifugal separator
US7022061B2 (en) 2002-10-15 2006-04-04 Andritz Ag Centrifuge discharge port with power recovery
US20040072668A1 (en) 2002-10-15 2004-04-15 Baker Hughes Incorporated Liquid phase discharge port incorporating chamber nozzle device for centrifuge
DK176946B1 (en) † 2007-05-09 2010-06-14 Alfa Laval Corp Ab Centrifugal separator and a liquid phase drain port element
DK200801846A (en) † 2008-12-30 2010-07-01 Alfa Laval Corp Ab A decanter centrifuge with a slide valve body
DE102010061563A1 (en) † 2010-12-27 2012-06-28 Gea Mechanical Equipment Gmbh Solid bowl centrifuge with overflow weir

Also Published As

Publication number Publication date
EP2659985A1 (en) 2013-11-06
EP2551019B2 (en) 2019-11-06
DK2659985T4 (en) 2020-02-03
DK2551019T4 (en) 2020-02-03
EP2551019A1 (en) 2013-01-30
EP2659985B2 (en) 2019-11-06
EP2551019B1 (en) 2016-09-14
DK2659985T3 (en) 2016-12-19
EP2659985B1 (en) 2016-09-14

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