EP1949966A1 - Solid wall helical centrifuge with pressure plate - Google Patents
Solid wall helical centrifuge with pressure plate Download PDFInfo
- Publication number
- EP1949966A1 EP1949966A1 EP08001302A EP08001302A EP1949966A1 EP 1949966 A1 EP1949966 A1 EP 1949966A1 EP 08001302 A EP08001302 A EP 08001302A EP 08001302 A EP08001302 A EP 08001302A EP 1949966 A1 EP1949966 A1 EP 1949966A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- screw
- blade
- baffle plate
- solid bowl
- centrifuge according
- 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.)
- Granted
Links
- 239000007787 solid Substances 0.000 title claims description 28
- 239000000463 material Substances 0.000 claims abstract description 9
- 210000000051 wattle Anatomy 0.000 claims 1
- 230000000694 effects Effects 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 238000009825 accumulation Methods 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 241000237858 Gastropoda Species 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 239000007790 solid phase Substances 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
- B04B1/20—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
- B04B2001/2041—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 baffles, plates, vanes or discs attached to the conveying screw
Definitions
- the invention relates to a solid bowl screw centrifuge with a baffle plate according to the preamble of claim 1.
- baffles With solid bowl centrifuges, the use of baffles causes a build-up effect that affects the flow in the axial direction. In addition to this desired effect, there is also an influence on the flow in the circumferential direction.
- the solids cake In order to achieve effective conveying of the solids which form a solids cake with the screw, it is necessary for the solids cake not to rotate with respect to the drum, but to glide as close to it as possible. Between the solids cake and the screw only a relative movement in the circumferential direction is fed.
- the invention has the object to solve the problem described above with simpler design means.
- the at least one or the window-like openings bring several advantages with it.
- the measure is structurally particularly simple to implement and inexpensive.
- the snail extends on either side of the baffle plate so that it is cut by it.
- FIG. 3 shows a known solid bowl screw centrifuge with a rotatable drum 1 with horizontal axis of rotation D.
- a rotatable with a differential speed to the drum 1 screw 2 is arranged, which has a helical screw blade 3, which is arranged on the outer circumference of a screw body 4.
- An inlet pipe 5 serves to feed a product to be processed via a distributor 6 into the drum 1.
- At least one liquid outlet 7 and a solids discharge 8 serve to discharge at least one liquid phase and at least one solid phase.
- baffle plate 9 On the worm body 4, at least one baffle plate 9 is arranged in addition to the screw 3, which is formed from a substantially completely around the worm body 4 circumferential ring or disc element here.
- the baffle plate 9 intersects in at least one peripheral region with the baffle plate 9, wherein wedge-shaped regions 10, 13 are formed between the baffle plate 9 and the screw blade 3.
- first wedge region 10 In the flow direction of the solids to the solids discharge axially "first" wedge region 10 according to the invention at least one window-like opening 11, preferably in the screw blade 3, formed, which allows a flow of material through the Scheckenblatt 3.
- a corresponding window-like opening 12 may be provided in a further wedge area 13, which is formed on the other side of the baffle plate 9 in the region in which it meets the worm blade 3.
- Each of the apertures 11, 12 is preferably formed such that in each case a web of material 14, 15 and 16, 17 of the screw blade 3 is still standing on the inner and / or outer circumference of the screw body 4.
- the outer material webs 14, 15 may be reinforced by welds or the like. To strengthen the construction and to avoid imbalances by higher mass in this area.
- the openings 11, 12 can also start directly on the outer circumference of the screw body and / or enforce it radially completely outwards.
- the distance of the edge of the apertures 10, 11 to the baffle plate should be particularly preferred 0 mm, preferably less than 10 mm.
Landscapes
- Centrifugal Separators (AREA)
Abstract
Description
Die Erfindung betrifft eine Vollmantel-Schneckenzentrifuge mit einer Stauscheibe nach dem Oberbegriff des Anspruchs 1.The invention relates to a solid bowl screw centrifuge with a baffle plate according to the preamble of claim 1.
Bei Vollmantel-Schneckenzentrifugen wird durch den Einsatz von Stauscheiben ein Aufstaueffekt bewirkt, der die Strömung in axialer Richtung betrifft. Neben diesem an sich gewünschten Effekt kommt es auch zu einer Beeinflussung der Strömung in Umfangsrichtung. Um eine effektive Förderung der Feststoffe, die einen Feststoffkuchen ausbilden, mit der Schnecke zu erreichen, ist es erforderlich, dass sich der Feststoffkuchen nicht gegenüber der Trommel dreht sondern möglichst an ihr gleitet. Zwischen dem Feststoffkuchen und der Schnecke findet nur eine Relativbewegung in Umfangsrichtung satt.With solid bowl centrifuges, the use of baffles causes a build-up effect that affects the flow in the axial direction. In addition to this desired effect, there is also an influence on the flow in the circumferential direction. In order to achieve effective conveying of the solids which form a solids cake with the screw, it is necessary for the solids cake not to rotate with respect to the drum, but to glide as close to it as possible. Between the solids cake and the screw only a relative movement in the circumferential direction is fed.
Bekannte Schneckenzentrifugen zeigen die
Nach der in
Inder gattungsgemäßen
Die Erfindung hat die Aufgabe, das vorstehend beschriebene Problem mit einfacheren konstruktiven Mitteln zu beheben.The invention has the object to solve the problem described above with simpler design means.
Die Erfindung löst diese Aufgabe durch den Gegenstand des Anspruchs 1.The invention solves this problem by the subject matter of claim 1.
Vorteilhafte Ausgestaltungen sind den Unteransprüchen zu entnehmen.Advantageous embodiments can be found in the dependent claims.
Der wenigstens eine oder die fensterartigen Durchbrüche bringen gleich mehrere Vorteile mit sich.The at least one or the window-like openings bring several advantages with it.
So wird auf einfache Weise die Ansammlung von Feststoffen im Keil vermieden. Hierdurch wird das aufzubringende Schneckendrehmoment verringert, was auch in einer geringeren Stromaufnahme resultiert. U.U. sind sogar kleinere Getriebe zwischen Antriebsmotor (nicht dargestellt) und Schnecke einsetzbar.This easily avoids the accumulation of solids in the wedge. As a result, the worm torque to be applied is reduced, which also results in a lower power consumption. U.U. even smaller gears between the drive motor (not shown) and worm can be used.
Darüber hinaus ergibt sich eine geringere mechanische Belastung der Wendel und sogar ein geringerer Verschleiß der Trommel im Bereich der Stauscheibe.In addition, there is a lower mechanical load on the coil and even less wear of the drum in the baffle plate.
Darüber hinaus ist die Maßnahme konstruktiv besonders einfach umzusetzen und kostengünstig.In addition, the measure is structurally particularly simple to implement and inexpensive.
Insgesamt werden die Verfahrenwerte verbessert.Overall, the process values are improved.
Die Schnecke erstreckt sich jeweils auf beiden Seiten der Stauscheibe, so dass sie von ihr geschnitten wird.The snail extends on either side of the baffle plate so that it is cut by it.
Wird eine mehrgängige Schnecke eingesetzt, sind mehrere Schneckenblätter vorhanden, wobei die Stauscheibe dann beide Schneckengänge schneidet.If a multi-start screw is used, several screw blades are present, whereby the baffle plate then cuts both screw threads.
In der
Nachfolgend wird die Erfindung unter Bezug auf die Zeichnung anhand eines Ausführungsbeispiels näher beschrieben. Es zeigt:
- Fig. 1a
- eine Draufsicht auf einen Bereich einer Schnecke einer erfindungsgemäßen Vollmantel-Schneckenzentrifuge;
- Fig. 1b
- einen Schnitt senkrecht zur Drehachse durch die Vollmantel-Schneckenzentrifuge aus
Fig. 1a ; und - Fig. 2a
- eine Draufsicht auf einen Bereich einer Schnecke einer bekannten Vollmantel-Schneckenzentrifuge;
- Fig. 2b
- einen Schnitt senkrecht zur Drehachse durch die Vollmantel-Schneckenzentrifuge aus
Fig. 2a ; und - Fig. 3
- eine schematische Darstellung einer Vollmantel-Schneckenzentrifuge nach dem Stand der Technik.
- Fig. 1a
- a plan view of a portion of a screw of a solid bowl screw centrifuge according to the invention;
- Fig. 1b
- a section perpendicular to the axis of rotation through the solid bowl screw centrifuge
Fig. 1a ; and - Fig. 2a
- a plan view of a portion of a screw of a known solid bowl screw centrifuge;
- Fig. 2b
- a section perpendicular to the axis of rotation through the solid bowl screw centrifuge
Fig. 2a ; and - Fig. 3
- a schematic representation of a solid bowl screw centrifuge according to the prior art.
Ein Zulaufrohr 5 dient zur Zuleitung eines zu verarbeitenden Produktes über einen Verteiler 6 in die Trommel 1. Wenigstens ein Flüssigkeitsablauf 7 und ein Feststoffaustrag 8 dienen zum Austrag wenigstens einer Flüssigkeits- und wenigstens einer Feststoffphase.An
Auf dem Schneckenkörper 4 ist ergänzend zur Schnecke 3 wenigstens eine Stauscheibe 9 angeordnet, die aus einem hier im wesentlichen vollständig um den Schneckenkörper 4 umlaufenden Ring bzw. Scheibenelement gebildet wird. Die Stauscheibe 9 kreuzt sich in wenigstens einem Umfangsbereich mit der Stauscheibe 9, wobei keilförmige Bereiche 10, 13 zwischen der Stauscheibe 9 und dem Schneckenblatt 3 gebildet werden.On the
Die Drehrichtung der Schnecke wird wiederum mit U bezeichnet und mit den Pfeilen P2 die Relativströmung gegenüber der Schnecke in weiter Entfernung von der Stauscheibe.The direction of rotation of the screw is again denoted by U and the arrows P 2, the relative flow relative to the screw at a distance from the baffle plate.
In dem in Strömungsrichtung der Feststoffe zum Feststoffaustrag axial "ersten" Keilbereich 10 ist erfindungsgemäß wenigstens ein fensterartiger Durchbruch 11, vorzugsweise in dem Schneckenblatt 3, ausgebildet, welcher einen Durchfluss von Material durch das Scheckenblatt 3 ermöglicht.In the flow direction of the solids to the solids discharge axially "first"
Derart bleibt die Funktion der Stauscheibe 9 erhalten. Es wird aber vermieden, dass im Keilbereich 10 zu hohe Kräfte auftreten. Da die Schnecke 3 durchströmt werden kann, findet in dem Keilbereich 10 keine Ansammlung von Feststoffen mehr statt.Thus, the function of the
Ein entsprechender fensterartiger Durchbruch 12 kann in einem weiteren Keilbereich 13 vorgesehen sein, der auf der anderen Seite der Stauscheibe 9 in dem Bereich ausgebildet ist, in dem sie auf das Schneckenblatt 3 trifft.A corresponding window-
Auch hier wird durch die Durchströmung eine Herabsetzung der auftretenden Kräfte erreicht.Again, a reduction of the forces occurring is achieved by the flow.
Jeder der Durchbrüche 11, 12 wird vorzugsweise derart ausgebildet, dass am Innen- und/oder Außenumfang des Schneckenkörpers 4 jeweils noch ein Materialsteg 14, 15 und 16, 17 des Schneckenblattes 3 stehen bleibt.Each of the
Die äußeren Materialstege 14, 15 können durch Aufschweißungen oder dgl. verstärkt sein, um die Konstruktion zu stärken und um durch höhere Masse in diesem Bereich Unwuchten zu vermeiden.The
Die Durchbrüche 11, 12 können aber auch direkt am Außenumfang des Schneckenkörpers ansetzen und/oder es radial vollständig nach außen hin durchsetzen.However, the
Vorzugweise grenzt der/grenzen die Durchbrüche 11, 12 ferner in Umfangsrichtung jeweils direkt an den jeweiligen Bereich 18, 19 an, in dem die Stauscheibe 9 mit dem Schneckenblatt 3 zusammentrifft. D.h., die Stauscheibe selbst bildet dann einen Teil des Randes der Durchbrüche 11, 12. Dies wird besonders bevorzugt, denn ist die Wirkung der Durchbrüche ist hier besonders vorteilhaft. Insgesamt sollte der Abstand des Randes der Durchbrüche 10, 11 zur Stauscheibe insofern besonders bevorzugt 0 mm, vorzugsweise weniger als 10 mm betragen.Preferably, the / limits the
- Trommeldrum
- 11
- Schneckeslug
- 22
- Schneckenblattscrew blade
- 33
- Schneckenkörperscrew body
- 44
- Zulaufrohrsupply pipe
- 55
- Verteilerdistributor
- 66
- Flüssigkeitsablaufliquid drain
- 77
- Feststoffaustragsolids
- 88th
- Stauscheibebaffle plate
- 99
- Bereicheareas
- 10, 1310, 13
- Durchbrüchebreakthroughs
- 11,1211.12
- Materialstegematerial webs
- 14, 15, 16, 1714, 15, 16, 17
- Bereicheareas
- 18, 1918, 19
- Drehachseaxis of rotation
- DD
- Drehrichtung der SchneckeDirection of rotation of the screw
- UU
- Pfeilearrows
- P1, P2 P 1 , P 2
Claims (8)
dadurch gekennzeichnet, dass
characterized in that
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102007003928A DE102007003928A1 (en) | 2007-01-26 | 2007-01-26 | Solid bowl centrifuge with a baffle plate |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1949966A1 true EP1949966A1 (en) | 2008-07-30 |
EP1949966B1 EP1949966B1 (en) | 2016-05-04 |
Family
ID=39295058
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP08001302.2A Active EP1949966B1 (en) | 2007-01-26 | 2008-01-24 | Solid wall helical centrifuge with pressure plate |
Country Status (2)
Country | Link |
---|---|
EP (1) | EP1949966B1 (en) |
DE (1) | DE102007003928A1 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102009001054A1 (en) | 2009-02-20 | 2010-09-02 | Hiller Gmbh | Solid bowl centrifuge with coarse outlet |
CN109225668A (en) * | 2018-09-26 | 2019-01-18 | 苏州星亿机械有限公司 | Horizontal spiral discharge sedimentation centrifuge |
CN113374613A (en) * | 2021-06-10 | 2021-09-10 | 合肥新沪屏蔽泵有限公司 | Turbine pipeline pump |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BE543072A (en) | ||||
US4245777A (en) | 1979-08-30 | 1981-01-20 | Pennwalt Corporation | Centrifuge apparatus |
DE4408717A1 (en) | 1994-03-15 | 1995-09-21 | Metallgesellschaft Ag | Composite element for coating the tip of screw feeder blades |
WO1997022411A1 (en) * | 1995-12-18 | 1997-06-26 | Alfa Laval Separation A/S | A decanter centrifuge |
WO2002005966A2 (en) | 2000-07-14 | 2002-01-24 | Alfa Laval Inc. | Decanter centrifuge having a heavy phase solids baffle |
DE10125096A1 (en) | 2001-05-23 | 2002-11-28 | Hiller Gmbh | Decanter centrifuge |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CH144065A (en) * | 1930-01-24 | 1930-12-15 | Ruesch Friedrich | Tool for cutting machine tools. |
-
2007
- 2007-01-26 DE DE102007003928A patent/DE102007003928A1/en not_active Ceased
-
2008
- 2008-01-24 EP EP08001302.2A patent/EP1949966B1/en active Active
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BE543072A (en) | ||||
US4245777A (en) | 1979-08-30 | 1981-01-20 | Pennwalt Corporation | Centrifuge apparatus |
DE4408717A1 (en) | 1994-03-15 | 1995-09-21 | Metallgesellschaft Ag | Composite element for coating the tip of screw feeder blades |
WO1997022411A1 (en) * | 1995-12-18 | 1997-06-26 | Alfa Laval Separation A/S | A decanter centrifuge |
WO2002005966A2 (en) | 2000-07-14 | 2002-01-24 | Alfa Laval Inc. | Decanter centrifuge having a heavy phase solids baffle |
DE10125096A1 (en) | 2001-05-23 | 2002-11-28 | Hiller Gmbh | Decanter centrifuge |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102009001054A1 (en) | 2009-02-20 | 2010-09-02 | Hiller Gmbh | Solid bowl centrifuge with coarse outlet |
WO2010097327A1 (en) | 2009-02-20 | 2010-09-02 | Hiller Gmbh | Solid bowl screw centrifuge having coarse material outlet in baffle plate |
CN109225668A (en) * | 2018-09-26 | 2019-01-18 | 苏州星亿机械有限公司 | Horizontal spiral discharge sedimentation centrifuge |
CN113374613A (en) * | 2021-06-10 | 2021-09-10 | 合肥新沪屏蔽泵有限公司 | Turbine pipeline pump |
CN113374613B (en) * | 2021-06-10 | 2024-06-04 | 合肥新沪屏蔽泵有限公司 | Turbine pipeline pump |
Also Published As
Publication number | Publication date |
---|---|
DE102007003928A1 (en) | 2008-08-07 |
EP1949966B1 (en) | 2016-05-04 |
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