EP0640398A2 - Centrifugeuse - Google Patents
Centrifugeuse Download PDFInfo
- Publication number
- EP0640398A2 EP0640398A2 EP94112821A EP94112821A EP0640398A2 EP 0640398 A2 EP0640398 A2 EP 0640398A2 EP 94112821 A EP94112821 A EP 94112821A EP 94112821 A EP94112821 A EP 94112821A EP 0640398 A2 EP0640398 A2 EP 0640398A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- peeling
- centrifuge
- liquid
- channel
- drum
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B11/00—Feeding, charging, or discharging bowls
- B04B11/08—Skimmers or scrapers for discharging ; Regulating thereof
- B04B11/082—Skimmers for discharging 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
-
- 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
Definitions
- the invention is directed to a centrifuge, in particular to a screw centrifuge, for the separation of liquid-solid mixtures, consisting of a centrifuge drum which is rotatably mounted about its longitudinal axis, with means for feeding the mixture to be separated into the centrifuge drum, with openings in the Centrifuge drum for the discharge of the separated heavy substances (solid) and with a peeling disc for the discharge of the light substances (liquid) from the centrifuge drum, wherein the peeling disc has at least one peeling channel which extends from the periphery of the peeling disc to the center of the peeling disc in one leads in the axial direction discharge channel.
- the focus is on dewatering the solid as a preliminary stage to thermal drying.
- the liquid phase flows out of the centrifuge over the weir plates of the centrifuge at high circumferential speed, during which a strong turbulence occurs with the gas (normally air) present in the centrifuge.
- each peeling channel is assigned a discharge channel, the effective cross section of which can be changed by means of a throttle body.
- the liquid volume flow discharged through the peeling channels can thus be regulated and adapted to the inlet quantities, so that it is ensured that the entry opening of the peeling channels always remain within the liquid.
- turbulence can continue to arise within the peeling channels, combined with the suction of gas (air), even with strong throttling behind the peeling disc and thus a small volume flow within the peeling channels.
- This has the advantage over the throttling behind the peeling disc, that the inlet cross-section is always adapted to the volume flow to be discharged and is not larger than necessary.
- the peeling channel is according to the invention in the direction of drum rotation, i. H. Crescent-shaped in the direction of liquid rotation and runs divergently from the inlet area on the periphery of the peeling disk to the outlet area in the center of the peeling disk. H. its cross-sectional area increases.
- the cross-sectional area ratio of the inlet area to the outlet area is advantageously less than 1, preferably less than 0.1.
- the inventive design of the peeling channel not only advantageously adapts the liquid volume flow to the quantity to be discharged with the aim that the inlet opening of the peeling channel is always immersed in the liquid and no gas (air) is sucked into the peeling channel, but rather in the liquid-containing kinetic energy is converted into potential energy in a soft course with high efficiency and liquid shocks and cavitation are largely suppressed by avoiding turbulence.
- the partial disks forming the peeling disks are advantageously arranged on tubes which are inserted into one another and which are guided axially from the outside into the centrifuge drum and can be rotated relative to one another from the outside. In this way, it is possible to change the cross-section of the peeling channel in a simple manner from the outside, even during operation of the centrifuge, by rotating the tubes, and thus to adapt the peeling channel to fluctuating operating states of the centrifuge.
- the inner tube is at the same time also the feed tube through which the mixture to be separated is fed into the centrifuge drum from the outside.
- Fig. 1 shows a screw centrifuge (10) with an elongated centrifuge drum (11) and a coaxial inside the centrifuge drum (11) rotating screw conveyor (12), with solids discharge openings (13) at the end of the conical part of the centrifuge drum (11) and with a peeling disc (14) arranged at the opposite end of the centrifuge drum (11) for discharging the liquid.
- the peeling disc (14) is formed from two individual discs (15, 16) which are arranged at a distance from one another on tubes (17, 24) which are inserted into one another, so that there is between the individual discs (15, 16) forms a gap.
- the individual disks (15, 16) have inner disks (18, 19) screwed on, which, due to their geometry (crescent-shaped contour) and arrangement on the individual disks, have a radial distance from one another and the gap formed by the individual disks (15, 16) partially fill out.
- These inner disks (18, 19) form the peeling channel (20) in connection with the individual disks (15, 16), which runs from the periphery of the peeling disk to the center of the peeling disk (14).
- the dimension of the peeling disc (20) is constant in the axial direction and corresponds to the distance between the individual discs (15, 16). In the radial direction, the dimension of the The peeling channel (20) is determined by the radial distance between the inner disks (18, 19), the crescent-shaped curvature of the two inner disks (18, 19) being designed so that the peeling channel (20) from the periphery of the peeling disk (14) to it Center wider and thus the cross section of the peeling channel (14) is constantly increasing.
- the individual disks (15, 16) forming the peeling disk (14) are placed on each of the nested tubes (17, 24) - in the exemplary embodiment shown, the single disk (15) on the tube (17) and the single disk (16) on the tube (24) - and firmly connected to them, for example by welding.
- the two nested pipes (17, 24) form a discharge channel (22) between them, which is connected to the peeling channel (20) and which functions - the discharge of the liquid - even when the pipes (17, 24) are rotated against each other maintains and is led out of the centrifuge drum (11) with the two tubes (17, 24).
- the tubes (17, 24) leading from the outside into the centrifuge drum (11) - the inner tube (17) serves as a feed tube for feeding the suspension to be separated in the direction of arrow 23 into the centrifuge drum (11) - can be rotated relative to one another from the outside and thus also the individual disks (15, 16) attached to the pipe reels (17, 24), whereby the radial distance of the inner disks (18, 19) arranged on individual disks (15, 16) and thus the cross section of the peeling channel (20) changes.
- the peeling disc (19) described in this exemplary embodiment consists of a total of four parts, the two individual discs (15, 16) on each of the inner discs (18, 19), the base area of which corresponds to approximately half of the one individual disc (15, 16) , is attached.
- Such a peeling disc (14) can be produced with simple means, in particular the shape of the peeling channel can be adapted to the requirements of the liquid to be discharged by simply replacing the inner discs (18, 19) with correspondingly differently shaped inner discs.
- the inner disks it is also possible to use more than two inner disks, the inner disks then being able to be arranged axially or radially next to one another. According to the invention, it is also possible to dispense entirely with the inner panes. In this latter case, the peeling channel contours must then be machined out of the individual disks by a metalworking process, for example by milling.
Landscapes
- Centrifugal Separators (AREA)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE4328369 | 1993-08-25 | ||
DE19934328369 DE4328369A1 (de) | 1993-08-25 | 1993-08-25 | Zentrifuge |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0640398A2 true EP0640398A2 (fr) | 1995-03-01 |
EP0640398A3 EP0640398A3 (fr) | 1995-05-31 |
Family
ID=6495844
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP94112821A Withdrawn EP0640398A3 (fr) | 1993-08-25 | 1994-08-17 | Centrifugeuse. |
Country Status (3)
Country | Link |
---|---|
EP (1) | EP0640398A3 (fr) |
JP (1) | JPH07163907A (fr) |
DE (1) | DE4328369A1 (fr) |
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5800332A (en) * | 1996-07-03 | 1998-09-01 | Hensley; Gary L. | Decanting centrifuge employing elements with differing rates of rotation |
US5971907A (en) * | 1998-05-19 | 1999-10-26 | Bp Amoco Corporation | Continuous centrifugal separator with tapered internal feed distributor |
WO2000041813A1 (fr) * | 1999-01-11 | 2000-07-20 | Westfalia Separator Ag | Centrifugeuse comportant deux disques de raclage |
WO2003024606A1 (fr) * | 2001-09-05 | 2003-03-27 | Westfalia Separator Ag | Dispositif racleur a disque d'evacuation de liquide d'un tambour de centrifugeuse |
US6986733B2 (en) * | 2001-10-02 | 2006-01-17 | Westfalia Separator Industry Gmbh | Solid bowl helical conveyor centrifuge with a pressurized housing |
US7056273B2 (en) * | 2002-05-29 | 2006-06-06 | Westfalia Separator Ag | Solid bowl screw centrifuge comprising a peeling disk, and method for the operation thereof |
US7255670B2 (en) * | 2004-03-04 | 2007-08-14 | Hutchison Hayes, L.P. | Three phase decanter centrifuge |
US7510519B2 (en) * | 2003-08-08 | 2009-03-31 | Westfalia Separator Ag | Solid bowl screw centrifuge comprising a centripetal pump with a throtting device |
US20100041535A1 (en) * | 2006-02-10 | 2010-02-18 | Westfalia Separator Ag | Solid-bowl screw centrifuge and process for its operation |
US20140341714A1 (en) * | 2013-04-23 | 2014-11-20 | Andritz Frautech S.R.L. | Device For Drawing Off Fluid Of A Centrifugation Device |
DE102018114843A1 (de) * | 2018-03-21 | 2019-09-26 | Gea Mechanical Equipment Gmbh | Zentrifuge mit einer Schälscheibe |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB494211A (en) * | 1936-12-10 | 1938-10-21 | Separator Ab | Improvements in paring or skimming devices for centrifugal separators |
EP0068869A2 (fr) * | 1981-06-30 | 1983-01-05 | Alfa-Laval Separation A/S | Centrifugeuse comportant un disque d'écumage pour l'évacuation d'une phase liquide |
DE3936150A1 (de) * | 1988-12-07 | 1990-06-13 | Nagema Veb K | Schaelscheibe fuer zentrifugalseparatoren |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1942490U (de) * | 1966-03-08 | 1966-07-14 | Flottweg Motoren Werk Dr Georg | Vollmantelzentrifuge mit einer schaelscheibe. |
DE3518885A1 (de) * | 1985-05-25 | 1986-11-27 | Bayer Ag, 5090 Leverkusen | Vollmantelschneckenzentrifuge mit nachklaervorrichtung |
DE3833063C1 (en) * | 1988-09-29 | 1989-10-05 | Westfalia Separator Ag, 4740 Oelde, De | Skimming disc for discharging fluids from centrifuge drums |
-
1993
- 1993-08-25 DE DE19934328369 patent/DE4328369A1/de not_active Withdrawn
-
1994
- 1994-08-17 EP EP94112821A patent/EP0640398A3/fr not_active Withdrawn
- 1994-08-25 JP JP22428094A patent/JPH07163907A/ja not_active Withdrawn
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB494211A (en) * | 1936-12-10 | 1938-10-21 | Separator Ab | Improvements in paring or skimming devices for centrifugal separators |
EP0068869A2 (fr) * | 1981-06-30 | 1983-01-05 | Alfa-Laval Separation A/S | Centrifugeuse comportant un disque d'écumage pour l'évacuation d'une phase liquide |
DE3936150A1 (de) * | 1988-12-07 | 1990-06-13 | Nagema Veb K | Schaelscheibe fuer zentrifugalseparatoren |
Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5800332A (en) * | 1996-07-03 | 1998-09-01 | Hensley; Gary L. | Decanting centrifuge employing elements with differing rates of rotation |
US5971907A (en) * | 1998-05-19 | 1999-10-26 | Bp Amoco Corporation | Continuous centrifugal separator with tapered internal feed distributor |
WO2000041813A1 (fr) * | 1999-01-11 | 2000-07-20 | Westfalia Separator Ag | Centrifugeuse comportant deux disques de raclage |
AU750491B2 (en) * | 1999-01-11 | 2002-07-18 | Westfalia Separator Ag | Centrifuge comprising two stripping discs |
US6623417B1 (en) * | 1999-01-11 | 2003-09-23 | Westfalia Separator Ag | Centrifuge having a rotatable sleeve and a restriction point |
WO2003024606A1 (fr) * | 2001-09-05 | 2003-03-27 | Westfalia Separator Ag | Dispositif racleur a disque d'evacuation de liquide d'un tambour de centrifugeuse |
US6986733B2 (en) * | 2001-10-02 | 2006-01-17 | Westfalia Separator Industry Gmbh | Solid bowl helical conveyor centrifuge with a pressurized housing |
US7056273B2 (en) * | 2002-05-29 | 2006-06-06 | Westfalia Separator Ag | Solid bowl screw centrifuge comprising a peeling disk, and method for the operation thereof |
US7510519B2 (en) * | 2003-08-08 | 2009-03-31 | Westfalia Separator Ag | Solid bowl screw centrifuge comprising a centripetal pump with a throtting device |
US7255670B2 (en) * | 2004-03-04 | 2007-08-14 | Hutchison Hayes, L.P. | Three phase decanter centrifuge |
US20100041535A1 (en) * | 2006-02-10 | 2010-02-18 | Westfalia Separator Ag | Solid-bowl screw centrifuge and process for its operation |
US8444541B2 (en) * | 2006-02-10 | 2013-05-21 | Gea Mechanical Equipment Gmbh | Solid-bowl centrifuge having a liquid discharge sealed such that a pond level in a separation space remains unchanged when pressurization occurs |
US20140341714A1 (en) * | 2013-04-23 | 2014-11-20 | Andritz Frautech S.R.L. | Device For Drawing Off Fluid Of A Centrifugation Device |
US9856879B2 (en) * | 2013-04-23 | 2018-01-02 | Andritz Frautech S.R.L. | Centrifugation device with adjustable vanes |
DE102018114843A1 (de) * | 2018-03-21 | 2019-09-26 | Gea Mechanical Equipment Gmbh | Zentrifuge mit einer Schälscheibe |
Also Published As
Publication number | Publication date |
---|---|
DE4328369A1 (de) | 1995-03-02 |
JPH07163907A (ja) | 1995-06-27 |
EP0640398A3 (fr) | 1995-05-31 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP2155353B1 (fr) | Séparateur à vis à pression | |
DE60110441T2 (de) | Förderschnecke für zentrifuge, zentrifuge und trennverfahren | |
DE2220535B1 (de) | Drehstroemungswirbler zur sichtung feinkoerniger partikel | |
EP0146852A1 (fr) | Broyeur agitateur | |
EP0640398A2 (fr) | Centrifugeuse | |
DE60318833T2 (de) | Dekantierzentrifuge | |
WO2003078070A1 (fr) | Centrifugeuse a vis sans fin | |
EP0638365B1 (fr) | Procédé et dispositif pour séparer des matières solides à grains fins en deux fractions granulométriques | |
DE9218957U1 (de) | Filtervorrichtung | |
DE1471630B2 (de) | Zweistufennaßwäscher zur Reinigung von Gasen | |
EP0504836B1 (fr) | Broyeur agitateur | |
DE3624086C2 (fr) | ||
DE60308015T2 (de) | Vorrichtung und verfahren zur trennung eines gemisches | |
DE1040459B (de) | Schleudertrommel mit einem Trommelraum von relativ grosser Laenge | |
DE69307835T2 (de) | Pumpengehäuse Vorrichtung | |
DE69312643T2 (de) | Zentrifugaltrenner | |
DE2840128A1 (de) | Wirbelstrom-abscheider fuer aufschlaemmungen | |
DE2013499A1 (de) | Anordnung für einen Zyklonenabscheider mit einer Entleerungskammer | |
EP1337344A1 (fr) | Essoreuse a vis sans fin, a bol plein, munie d'un distributeur | |
DE2220534C3 (de) | Drehströmungswirbler zur Sichtung und Abscheidung feinkörniger Partikel | |
DE4029252A1 (de) | Verfahren und vorrichtung zum kontinuierlichen feinzerkleinern und dispergieren von feststoffen in fluessigkeit | |
DE19738912A1 (de) | Vorrichtung und Verfahren zum Abscheiden von Feststoffen aus einem Trägerstrom sowie deren Verwendung | |
AT211288B (de) | Gaszentrifuge | |
DE1197812B (de) | Vollmantel-Schneckenzentrifuge zum Abscheiden von Feststoffteilchen aus Fluessigkeiten | |
DE1432772B2 (de) | Fliehkraftabscheider fuer eine fluessigkeitsbetriebene schleuderstrahlanlage |
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 |
|
AK | Designated contracting states |
Kind code of ref document: A2 Designated state(s): DE DK ES IT NL SE |
|
PUAL | Search report despatched |
Free format text: ORIGINAL CODE: 0009013 |
|
AK | Designated contracting states |
Kind code of ref document: A3 Designated state(s): DE DK ES IT NL SE |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE APPLICATION IS DEEMED TO BE WITHDRAWN |
|
18D | Application deemed to be withdrawn |
Effective date: 19951201 |