EP0252341A2 - Centrifuge à tamis travaillant en continu avec entraînement par le haut - Google Patents

Centrifuge à tamis travaillant en continu avec entraînement par le haut Download PDF

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Publication number
EP0252341A2
EP0252341A2 EP87108663A EP87108663A EP0252341A2 EP 0252341 A2 EP0252341 A2 EP 0252341A2 EP 87108663 A EP87108663 A EP 87108663A EP 87108663 A EP87108663 A EP 87108663A EP 0252341 A2 EP0252341 A2 EP 0252341A2
Authority
EP
European Patent Office
Prior art keywords
drum
centrifuge
centrifugal
drums
sugar
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
Application number
EP87108663A
Other languages
German (de)
English (en)
Other versions
EP0252341B1 (fr
EP0252341A3 (en
Inventor
Bernhard Fiedler
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.)
BWS Technologie GmbH
Original Assignee
Dorr Oliver Deutschland GmbH
Fried Krupp AG
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 Dorr Oliver Deutschland GmbH, Fried Krupp AG filed Critical Dorr Oliver Deutschland GmbH
Priority to AT87108663T priority Critical patent/ATE94425T1/de
Publication of EP0252341A2 publication Critical patent/EP0252341A2/fr
Publication of EP0252341A3 publication Critical patent/EP0252341A3/de
Application granted granted Critical
Publication of EP0252341B1 publication Critical patent/EP0252341B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04BCENTRIFUGES
    • B04B3/00Centrifuges with rotary bowls in which solid particles or bodies become separated by centrifugal force and simultaneous sifting or filtering

Definitions

  • the invention relates to a continuously operating sieve centrifuge, in particular a sugar centrifuge with two centrifugal drums arranged one above the other and connected to one another, each of which is connected to a centrifugal shaft rotating and driven about a vertical axis and both centrifugal drums are accommodated in a common housing.
  • the invention has for its object to provide a centrifuge of the type mentioned, with which the pre-spin compared to the post-spin is subject to a greater or the same size separation effect with the smallest footprint and washed and removed the centrifuge separately in both spin stages, and between the first and second Centrifugation a mashing can be provided. Furthermore, the aim is to avoid as far as possible the unbalances resulting from the unavoidable unequal distribution of the filling materials and to separate the green runoff and white runoff.
  • a centrifuge housing 1 with a centrifuge lid 2 and a centrifuge bottom 3 is one Cylinder wall 5 is provided for collecting the white drain separately from the green drain. Furthermore, a stop bushing 13 is provided on the centrifuge bottom 3, in which the centrifuge shaft 9 rotates freely without a guide, but which limits the deflection of the shaft in order to prevent the drum from striking. A movable air seal 13 is provided on the centrifuge lid 2, which prevents the entry of external air, but does not hinder the free movement of the centrifuge shaft 9 with regard to self-centering. At the upper end of the centrifuge shaft 9 there is a self-aligning bearing 14 with a motor 12 arranged above it.
  • the upper centrifugal drum 15 is fastened by means of a hub 16, on which there is a drum base 17 with a drum jacket 18 which is flared upwards.
  • an accelerator cone 19 is connected to the hub 16, an accelerator pot 36 of the accelerator cone 19 being filled from a filling device 20.
  • the filling compound reaches the lower area of the drum casing 18 and travels over the inside thereof to the outlet flange 21, where the dry-spun sugar is discharged.
  • a washing device 22 with nozzles sprays a washing liquid onto the migrating sugar layer, whereby the degree of purity of the sugar is increased.
  • the centrifuged mother syrup reaches a gutter 24 and is discharged via a discharge line 25.
  • the spun off sugar goes into channel 4.
  • the lower centrifugal drum 26 is fastened to the centrifuge shaft by means of a hub 39, wherein a spacer tube 30 is provided between the two centrifugal drums.
  • a spacer tube 30 is provided between the two centrifugal drums.
  • a washing device 31 is also inserted into the lower centrifugal drum.
  • the sugar spun out of the upper centrifugal drum 15 is subjected to a mashing liquid, for example a syrup of higher purity, and mashed in via a device 23 in the region of the outlet flange 21.
  • the sugar mass mashed into channel 4 in this way reaches the accelerator device 34 of the lower centrifugal drum 26 via a line 6.
  • the sugar layer migrates over the inside of the drum casing 28 and is thereby washed by means of the washing device 31.
  • the spun-off sugar thus reaches the annular space 35 via the outlet flange 29.
  • the spun-off syrup is collected on the inside of the cylinder plate 5 and collected in an annular space 7 formed by a further ring plate 8 and via the opening 37 and the line 32 and / or 10 dissipated.
  • the sugar discharged from the lower centrifugal drum 26 can be discharged dry and in this case is collected by the inner wall of the housing 1 and fed to a sugar failure channel 33.
  • the sugar discharged from the lower centrifugal drum 26 can also be mashed in.
  • the lines required for mashing and dissolving to supply the corresponding liquids are not shown because these devices are known per se. Both the mashed-in and the dissolved sugar are withdrawn via appropriate means, not shown, via channel 33.
  • the essence of the invention is to be seen in the fact that a filling compound can be spun twice in the smallest footprint and mashed in between the individual spinning processes, the transfer of the pre-spun and mashed sugar taking place automatically via mechanical devices.
  • the proposed solution avoids unbalance with all its disadvantageous consequences due to the novel arrangement of the drive, drums and bearings.
  • the pendulum suspended double drums work as a self-stabilizing gyro. Imbalances caused by unevenly distributed centrifugal material (filling mass) are compensated for by moving the centrifuge axis. The centrifuge runs more quietly than centrifuges with centrifugal drums that are positively driven.
  • the supply of the crystals spun off in the upper drum and mashed in with liquid via a single or multi-course straight or spiral channel to the accelerator pot of the lower drum ensures a screen spinner control using a stroboscope during production. This is particularly advantageous, since it allows the flow behavior to be observed and can be favorably influenced by appropriate regulation of the addition of syrup. This ensures a uniform and better quality of the end product.
  • Another advantage of the invention is that the replacement of damaged deck screens in the lower drum is possible in this embodiment without dismantling the centrifuge. Downtimes and the associated loss of production are reduced to a minimum.
  • Another advantage of the invention that cannot be overlooked is that energy can be saved by freely exchanging the rotating air masses from the upper and lower drums and vice versa compared to arranging the drums in separate rooms.

Landscapes

  • Centrifugal Separators (AREA)
EP87108663A 1986-07-09 1987-06-16 Centrifuge à tamis travaillant en continu avec entraînement par le haut Expired - Lifetime EP0252341B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT87108663T ATE94425T1 (de) 1986-07-09 1987-06-16 Kontinuierlich arbeitende siebzentrifuge mit obenliegendem antrieb.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE3622959 1986-07-09
DE3622959A DE3622959C2 (de) 1986-07-09 1986-07-09 Kontinuierlich arbeitende Siebzentrifuge mit obenliegendem Antrieb

Publications (3)

Publication Number Publication Date
EP0252341A2 true EP0252341A2 (fr) 1988-01-13
EP0252341A3 EP0252341A3 (en) 1989-11-08
EP0252341B1 EP0252341B1 (fr) 1993-09-15

Family

ID=6304675

Family Applications (1)

Application Number Title Priority Date Filing Date
EP87108663A Expired - Lifetime EP0252341B1 (fr) 1986-07-09 1987-06-16 Centrifuge à tamis travaillant en continu avec entraînement par le haut

Country Status (4)

Country Link
EP (1) EP0252341B1 (fr)
AT (1) ATE94425T1 (fr)
DE (1) DE3622959C2 (fr)
HU (1) HU203991B (fr)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4725788A (en) * 1985-09-28 1988-02-16 Licentia Patent-Verwaltungs-Gmbh Switching amplifier
US5300013A (en) * 1989-10-04 1994-04-05 Dorr-Oliver Deutschland Gmbh Double centrifuge for highly viscous material
EP0692311A1 (fr) * 1994-07-15 1996-01-17 Braunschweigische Maschinenbauanstalt AG Centrifugeuse travaillant en continu pour la centrifugation de masses cuites
RU2132234C1 (ru) * 1995-06-27 1999-06-27 Киреев Виктор Иванович Прецессионный центробежный сепаратор
RU2132736C1 (ru) * 1995-06-27 1999-07-10 Киреев Виктор Иванович Способ разделения зернистых материалов
GB2539466A (en) * 2015-06-17 2016-12-21 Mann & Hummel Gmbh Centrifugal separator
RU2668616C1 (ru) * 2017-09-21 2018-10-02 Закрытое акционерное общество "ИТОМАК" Центробежный концентратор камерного типа

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102016008255B3 (de) 2016-07-10 2017-08-03 Wenker Gmbh & Co. Kg Verfahren und Vorrichtung zur Wiedergewinnung von Spritznebeln aus Spritzlackierkabinen
DE102017002312B3 (de) 2017-03-10 2017-11-23 Wenker Gmbh & Co. Kg Verfahren und Vorrichtung zur Wiedergewinnung von Spritzlacken aus Spritznebeln von Spritzlackierkabinen
DE102017007329B4 (de) 2017-08-04 2023-07-27 Wenker Gmbh & Co. Kg Verfahren und Vorrichtung zur Wiedergewinnung von Spritzlacken aus Spritznebeln von Spritzlackierkabinen

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE398102C (de) * 1924-07-08 Joseph Avrutik Vorrichtung zum Trennen von Gemischen aus festen und fluessigen Bestandteilen, insbesondere von Zuckerkristallen und Mutterlauge
GB161822A (en) * 1920-03-26 1921-04-21 Frederick William Fischlein Improvements in centrifugal apparatus for straining liquids
US1839941A (en) * 1927-03-29 1932-01-05 Zelezniak Wladyslaw Centrifugal separator
DE1915980B2 (de) * 1968-05-09 1972-10-26 Officine Meccaniche e Fonderie A. Bosco S.p.A., Terni (Italien) Kontinuierlich arbeitende Zentri fuge mit pendelnd aufgehängter Schleudertrommel
DE2025828C3 (de) * 1970-05-27 1980-07-10 Maschinenfabrik Buckau R. Wolf Ag, 4048 Grevenbroich Kontinuierlich arbeitende Zentrifuge, insbes. Zuckerzentrifuge
DE2849927B2 (de) * 1978-11-17 1980-11-27 Maschinenfabrik Buckau R. Wolf Ag, 4048 Grevenbroich Kontinuierlich arbeitende Zucker-Zentrifuge mit einer Einmaischvorrichtung
DE2948691C2 (de) * 1979-12-04 1984-11-15 Braunschweigische Maschinenbauanstalt AG, 3300 Braunschweig Kontinuierlich arbeitende Zentrifuge zum Einmaischen und Abschleudern von Zuckerfüllmassen
DE3415519A1 (de) * 1984-04-26 1985-10-31 Fried. Krupp Gmbh, 4300 Essen Kontinuierlich arbeitende siebzentrifuge

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4725788A (en) * 1985-09-28 1988-02-16 Licentia Patent-Verwaltungs-Gmbh Switching amplifier
US5300013A (en) * 1989-10-04 1994-04-05 Dorr-Oliver Deutschland Gmbh Double centrifuge for highly viscous material
EP0692311A1 (fr) * 1994-07-15 1996-01-17 Braunschweigische Maschinenbauanstalt AG Centrifugeuse travaillant en continu pour la centrifugation de masses cuites
US5618352A (en) * 1994-07-15 1997-04-08 Braunschweigische Maschinenbauanstalt Ag Continuously operating centrifuge for spinning sugar massecuite
RU2132234C1 (ru) * 1995-06-27 1999-06-27 Киреев Виктор Иванович Прецессионный центробежный сепаратор
RU2132736C1 (ru) * 1995-06-27 1999-07-10 Киреев Виктор Иванович Способ разделения зернистых материалов
GB2539466A (en) * 2015-06-17 2016-12-21 Mann & Hummel Gmbh Centrifugal separator
GB2539466B (en) * 2015-06-17 2020-10-21 Mann & Hummel Gmbh Centrifugal separator
RU2668616C1 (ru) * 2017-09-21 2018-10-02 Закрытое акционерное общество "ИТОМАК" Центробежный концентратор камерного типа

Also Published As

Publication number Publication date
EP0252341B1 (fr) 1993-09-15
ATE94425T1 (de) 1993-10-15
DE3622959C2 (de) 1996-12-12
DE3622959A1 (de) 1988-01-21
EP0252341A3 (en) 1989-11-08
HU203991B (en) 1991-11-28
HUT47226A (en) 1989-02-28

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