WO1991012081A1 - Zentrifuge mit einer selbstentleerenden schleudertrommel - Google Patents

Zentrifuge mit einer selbstentleerenden schleudertrommel Download PDF

Info

Publication number
WO1991012081A1
WO1991012081A1 PCT/EP1991/000114 EP9100114W WO9112081A1 WO 1991012081 A1 WO1991012081 A1 WO 1991012081A1 EP 9100114 W EP9100114 W EP 9100114W WO 9112081 A1 WO9112081 A1 WO 9112081A1
Authority
WO
WIPO (PCT)
Prior art keywords
line
centrifuge
emptying
valve
self
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.)
Ceased
Application number
PCT/EP1991/000114
Other languages
German (de)
English (en)
French (fr)
Inventor
Karl-Heinz Zettier
Siegfried Smigielski
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
GEA Mechanical Equipment GmbH
Original Assignee
Westfalia Separator GmbH
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Westfalia Separator GmbH filed Critical Westfalia Separator GmbH
Priority to EP91902695A priority Critical patent/EP0515396B1/de
Priority to DE59101726T priority patent/DE59101726D1/de
Publication of WO1991012081A1 publication Critical patent/WO1991012081A1/de
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04BCENTRIFUGES
    • B04B11/00Feeding, charging, or discharging bowls
    • B04B11/02Continuous feeding or discharging; Control arrangements therefor

Definitions

  • the invention relates to a centrifuge with a self-emptying centrifugal drum, to which the product to be centrifuged is fed via an inlet line, at least one liquid phase being drained under pressure from the centrifugal drum via an outlet line and solids accumulating in the centrifugal drum being discharged in predeterminable time intervals .
  • centrifuges are generally known. So-called partial evacuations can be carried out in order to expel the solids, in which only a small part of the waste contents is evacuated. This process leads to a sudden drop in pressure in the drum and thus also in the drain line. This can have a negative effect on the operation of downstream equipment.
  • the object of the invention is to develop the known centrifuge in such a way that even when the centrifuge is partially emptied, there is no pressure drop in the discharge line.
  • the drain line is provided with an elastic line part which is surrounded by a housing in an airtight manner, and the housing is connected to a pressure source via a line with a valve arranged therein.
  • the valve Before a partial evacuation is triggered, the valve is first opened and the elastic line part is thereby subjected to pressure. If the pressure drop described occurs in the drainage line during the subsequent partial emptying, the elastic line part is compressed by the pressure applied from the outside and displaces part of the product volume present in it, which corresponds to the solid quantity expelled. The pressure drop is compensated for by this process.
  • the elastic line part is provided in a bypass line.
  • the line part intended for product discharge can then consist of solid material as usual.
  • valves are arranged in the drain line and the bypass line in this way. arranges that the drain from the centrifuge can optionally be routed exclusively via one of the two lines. This arrangement offers particular advantages when it comes to cleaning the circuit of the lines.
  • the centrifuge has a second drain line
  • the valve is opened and product is briefly conveyed from the inlet into the second discharge line.
  • Compressed air is preferably used as the pressure medium.
  • the centrifuge to which the product to be centrifuged is fed via a feed line 2 is denoted by 1.
  • the liquid phases separated from one another in the centrifuge are discharged via the discharge line 3 and the second discharge line 4.
  • the drain line 3 is provided with a bypass line 5 in which there is an elastic Line part 6 is located, which is surrounded airtight by a housing 7 which is connected to a pressure source 10 via a line 8 with a valve 9 provided therein.
  • a valve 11 is arranged in the drain line 3 and a valve 12 is arranged in the bypass line 5.
  • the inlet line 2 is connected to the outlet line 4 via a second bypass line 13 in which a valve 14 is provided.
  • the centrifuge When the centrifuge is charged with product via the inlet 2, the separated liquid phases are discharged under pressure via the outlet line 3 and the second outlet line 4.
  • the optimum pressure in each case is set by devices not shown.
  • the valve 9 Before the partial emptying, the valve 9 is first opened and thereby the housing 7 is pressurized and thus also the elastic line part 6 Product flows back into the drum. The amount flowing back is replaced by product which is located in the elastic conduit part 6, because this is compressed when the pressure begins to fall in the discharge conduit 3 due to the pressure difference that then arises.
  • the valve 14 in the second bypass line 13 is also opened during the emptying process. Since the pressure drop caused by emptying is only present for approx. 1 second, the brief product inflow into the second discharge line 4 is tolerable in many cases. After completion of the emptying process, the bypass line is filled by 5 * a connecting line 15 again.
  • bypass line 5 and the drain line 3 can be rinsed separately by appropriate switching of the valves 11 and 12 in order to improve the cleaning effect.

Landscapes

  • Centrifugal Separators (AREA)
PCT/EP1991/000114 1990-02-14 1991-01-22 Zentrifuge mit einer selbstentleerenden schleudertrommel Ceased WO1991012081A1 (de)

Priority Applications (2)

Application Number Priority Date Filing Date Title
EP91902695A EP0515396B1 (de) 1990-02-14 1991-01-22 Zentrifuge mit einer selbstentleerenden schleudertrommel
DE59101726T DE59101726D1 (de) 1990-02-14 1991-01-22 Zentrifuge mit einer selbstentleerenden schleudertrommel.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE4004459A DE4004459C2 (de) 1990-02-14 1990-02-14 Verfahren zum Betreiben einer Zentrifuge mit einer selbstentleerenden Schleudertrommel und Zentrifuge zur Durchführung des Verfahrens
DEP4004459.9 1990-02-14

Publications (1)

Publication Number Publication Date
WO1991012081A1 true WO1991012081A1 (de) 1991-08-22

Family

ID=6400074

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/EP1991/000114 Ceased WO1991012081A1 (de) 1990-02-14 1991-01-22 Zentrifuge mit einer selbstentleerenden schleudertrommel

Country Status (6)

Country Link
US (1) US5267937A (https=)
EP (1) EP0515396B1 (https=)
DE (2) DE4004459C2 (https=)
DK (1) DK0515396T3 (https=)
IE (1) IE66728B1 (https=)
WO (1) WO1991012081A1 (https=)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1996034693A1 (en) * 1995-05-02 1996-11-07 Tetra Laval Holdings & Finance S.A. Method and centrifugal separator for separation of two liquids

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2301697B (en) * 1995-06-01 1999-04-07 Ronald Howard Brewis Harmonica tuning system
US6906172B2 (en) * 1998-03-10 2005-06-14 Large Scale Biology Corporation Flexible processing apparatus for isolating and purifying viruses, soluble proteins and peptides from plant sources
US9220295B2 (en) 2010-12-01 2015-12-29 R.J. Reynolds Tobacco Company Tobacco separation process for extracting tobacco-derived materials, and associated extraction systems
US9661876B2 (en) 2013-03-14 2017-05-30 R.J. Reynolds Tobacco Company Sugar-enriched extract derived from tobacco
US9301544B2 (en) 2013-03-14 2016-04-05 R.J. Reynolds Tobacco Company Protein-enriched tobacco-derived composition
DE102015119165B4 (de) * 2015-11-06 2022-06-09 Gea Mechanical Equipment Gmbh Verfahren zur Klärung eines fließfähigen Produktes mit einer Zentrifuge, insbesondere einem Separator
DE102017115112A1 (de) 2017-07-06 2019-01-10 Gea Mechanical Equipment Gmbh Anlage zur zentrifugalen Klärung einer Suspension

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1023726B (de) * 1956-08-02 1958-01-30 Westfalia Separator Ag Zulaufeinrichtung fuer Milchzentrifugen zum Einstellen verschiedener konstanter Leistungen
FR1481803A (fr) * 1966-06-02 1967-05-19 Westfalia Separator Ag Dispositif pour maintenir constant le rapport quantitatif de constituants extraits d'un liquide au moyen d'un séparateur centrifuge
DE2151475A1 (de) * 1971-10-15 1973-04-19 Kurt Pause Kontinuierlich arbeitende dickschichtstroemungszentrifuge mit einer schichtdickenregelung

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5437964A (en) * 1977-08-30 1979-03-20 Mitsubishi Kakoki Kk Centrifugal separator
DE3340636A1 (de) * 1983-11-10 1985-05-23 Krauss-Maffei AG, 8000 München Verfahren und vorrichtung zum pneumatischen entleeren von zentrifugen
DE3539485A1 (de) * 1985-11-07 1987-05-21 Alfa Laval Ind Tech Verfahren zur steuerung einer milchverarbeitungsvorrichtung

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1023726B (de) * 1956-08-02 1958-01-30 Westfalia Separator Ag Zulaufeinrichtung fuer Milchzentrifugen zum Einstellen verschiedener konstanter Leistungen
FR1481803A (fr) * 1966-06-02 1967-05-19 Westfalia Separator Ag Dispositif pour maintenir constant le rapport quantitatif de constituants extraits d'un liquide au moyen d'un séparateur centrifuge
DE2151475A1 (de) * 1971-10-15 1973-04-19 Kurt Pause Kontinuierlich arbeitende dickschichtstroemungszentrifuge mit einer schichtdickenregelung

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1996034693A1 (en) * 1995-05-02 1996-11-07 Tetra Laval Holdings & Finance S.A. Method and centrifugal separator for separation of two liquids

Also Published As

Publication number Publication date
DK0515396T3 (da) 1994-09-26
IE910273A1 (en) 1991-08-14
IE66728B1 (en) 1996-01-24
DE4004459C2 (de) 1995-08-31
DE4004459C1 (https=) 1991-03-07
EP0515396A1 (de) 1992-12-02
DE59101726D1 (de) 1994-06-30
US5267937A (en) 1993-12-07
EP0515396B1 (de) 1994-05-25

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