GB1315250A - Centrifugal separators - Google Patents
Centrifugal separatorsInfo
- Publication number
- GB1315250A GB1315250A GB5575271A GB5575271A GB1315250A GB 1315250 A GB1315250 A GB 1315250A GB 5575271 A GB5575271 A GB 5575271A GB 5575271 A GB5575271 A GB 5575271A GB 1315250 A GB1315250 A GB 1315250A
- Authority
- GB
- United Kingdom
- Prior art keywords
- liquid
- conduit
- rotor
- separated
- sediment
- 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.)
- Expired
Links
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
- B04B1/10—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with discharging outlets in the plane of the maximum diameter of the bowl
- B04B1/14—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with discharging outlets in the plane of the maximum diameter of the bowl with periodical discharge
- B04B1/16—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with discharging outlets in the plane of the maximum diameter of the bowl with periodical discharge with discharging outlets controlled by the rotational speed of the bowl
- B04B1/18—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with discharging outlets in the plane of the maximum diameter of the bowl with periodical discharge with discharging outlets controlled by the rotational speed of the bowl controlled by the centrifugal force of an auxiliary liquid
-
- 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
- B04B11/02—Continuous feeding or discharging; Control arrangements therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B13/00—Control arrangements specially designed for centrifuges; Programme control of centrifuges
Landscapes
- Centrifugal Separators (AREA)
Abstract
1315250 Centrifugal separator ALFA LAVAL AB 1 Dec 1971 [7 Dec 1970] 55752/71 Heading B2P A centrifugal separator for separating a mixture into a liquid component and sediment comprises a rotor 1, 2, Fig. 1, an inlet 5 for the mixture to be separated, an outlet 16 for the separated liquid, valve means 12 for controlling the discharge of sediment from an outlet 11 at the periphery of the rotor, means 27, 28, Fig. 2, for supplying the rotor with a further liquid the density of which is greater than the separated liquid and less than the sediment so that in use an interface is formed between said further denser liquid and the separated liquid, and means 31 for sensing the arrival of said interface at a predetermined radial level when it moves within the rotor, the arrangement being such that when the interface is at the predetermined level the rinsing means operates to actuate the valve means and open the peripheral outlet. The inlet 5 is constituted by a central duct through the drive shaft 4 of the rotor. The mixture is directed by a distributor 7 provided with vanes 6 into the separating chamber 8 in which conical plates 9 are mounted. The valve means or disc 12, which forms the bottom of the chamber, is operable to open or close the sediment outlets 11 by liquid supplied to a space 14 underneath the disc 12 through a supply chamber 13, throttled openings 15 being provided for the escape of the operating liquid. The separated liquid component leaving the chamber 8 through the outlet 16 flows into a chamber 17 from which it is pumped by a paring disc 18 through an outlet conduit 19. A duct 20 extends inwardly towards a chamber 21 from which liquid is pumped by a paring disc 22 through an outlet conduit 23. The conduit 23 is connected to an inlet conduit 24 directly connected to the duct 5 and contains a throttle 26. The denser liquid is supplied by a pump 28 through a conduit 27 connected to the inlet conduit 24. The sensing means 31 is connected to the conduit 23 and through a connection 30 feeds to a control equipment 29, which controls the opening and closing of the sediment outlets 11, information about a certain indication made of the liquid flow in the conduit 23. This indication can be the liquid pressure, the magnitude of the flow or the dielectric constant of the liquid flowing through the conduit 23. When pressure is indicated, however, no flow of liquid is necessary through the conduit 23 which may be closed off beyond the sensing means 31. The position of the interface 32 may alternatively be sensed by means of members placed within or at the outside of the rotor. In operation, the rotor is charged with the mixture and simultaneously the denser liquid is fed to it by the pump 28 through the conduits 27 and 24. An interface 32 is formed between the separated liquid component and the denser liquid. While the separated liquid leaves the rotor chamber 8 through the outlet 16, the interface 32 moves radially inwards due to an increase in the amount of denser liquid and of separated sediment. When the interface is situated radially outside the opening of the duct 20, the separated (lighter) liquid component discharges through the duct 20 and the conduit 23. When the interface reaches the opening of the duct 20 the pressure therein drops and the denser liquid flow through the conduit. This condition is sensed by the sensing means 31 which transmits a signal to the control equipment 29 and, the latter causes the outlets 11 to be opened so that separated sediment is discharged. Instead of supplying the denser liquid continuously to the rotor, a predetermined amount may be supplied after each time the outlets 11 have been opened. In this case the time interval between successive openings of the outlets 11 will depend entirely upon the sediment content of the mixture.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SE16514/70D SE345603B (en) | 1970-12-07 | 1970-12-07 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1315250A true GB1315250A (en) | 1973-05-02 |
Family
ID=20302366
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB5575271A Expired GB1315250A (en) | 1970-12-07 | 1971-12-01 | Centrifugal separators |
Country Status (8)
Country | Link |
---|---|
US (1) | US3750940A (en) |
JP (1) | JPS5648217B1 (en) |
DE (1) | DE2160476A1 (en) |
FR (1) | FR2117188A5 (en) |
GB (1) | GB1315250A (en) |
IT (1) | IT941789B (en) |
SE (1) | SE345603B (en) |
SU (1) | SU597323A3 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2139121A (en) * | 1983-04-23 | 1984-11-07 | Westfalia Separator Ag | Centrifugal cleaning of used mineral oils |
GB2185425A (en) * | 1986-01-22 | 1987-07-22 | Westfalia Separator Ag | Regulating operation of a centrifuge |
Families Citing this family (24)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA1125248A (en) * | 1976-09-03 | 1982-06-08 | John Novoselac | Centrifuge apparatus and method of operating a centrifuge |
US4347971A (en) * | 1977-03-03 | 1982-09-07 | Joy Manufacturing Company | Centrifuge apparatus |
US4350282A (en) * | 1980-12-23 | 1982-09-21 | Donaldson Company, Inc. | Self-purging centrifuge |
US4392846A (en) * | 1981-05-18 | 1983-07-12 | Joy Manufacturing Company | Centrifuge apparatus |
DE3228074A1 (en) * | 1982-07-28 | 1984-02-02 | Westfalia Separator Ag, 4740 Oelde | METHOD AND DEVICE FOR OPTIMIZING THE CLEARED PHASE AND THE SOLID CONCENTRATION IN A CENTRIFUGE WITH CONTINUOUS SOLID OUTPUT |
SE8302215D0 (en) * | 1983-04-20 | 1983-04-20 | Alfa Laval Marine Power Eng | centrifugal |
SE445809B (en) * | 1984-12-12 | 1986-07-21 | Alfa Laval Ab | DEVICE FOR REGULATING THE OUTPUT OF A SEPARATED COMPONENT FROM A Centrifugal Separator |
SE445892B (en) * | 1984-12-12 | 1986-07-28 | Alfa Laval Ab | OUTPUT DEVICE BY A Centrifugal Separator |
US4643709A (en) * | 1985-05-01 | 1987-02-17 | Alfa-Laval, Inc. | Method of operating nozzle centrifuges |
DE3603385C1 (en) * | 1986-02-05 | 1987-06-04 | Westfalia Separator Ag | Continuous centrifugal drum for concentrating suspended solids |
US5318500A (en) * | 1992-10-15 | 1994-06-07 | Eli Lilly And Company | Method for controlling intermittently discharged centrifuges |
SE503017C2 (en) * | 1994-07-22 | 1996-03-11 | Tetra Laval Holdings & Finance | Method and apparatus for monitoring centrifugal separator |
US6607473B2 (en) * | 1999-08-06 | 2003-08-19 | Econova Inc. | Methods for centrifugally separating mixed components of a fluid stream under a pressure differential |
US6719681B2 (en) | 1999-08-06 | 2004-04-13 | Econova, Inc. | Methods for centrifugally separating mixed components of a fluid stream |
US6346069B1 (en) | 1999-08-06 | 2002-02-12 | Separation Process Technology, Inc. | Centrifugal pressurized separators and methods of controlling same |
EP1487585B1 (en) * | 2002-01-25 | 2009-04-29 | Econova Inc. | Centrifugally separating mixed components of a fluid stream |
SE528387C2 (en) * | 2005-03-08 | 2006-10-31 | Alfa Laval Corp Ab | Centrifugal separator and method for separating a product into at least a relatively heavy phase and a relatively light phase |
DE202007009212U1 (en) * | 2007-06-30 | 2008-12-11 | Gea Westfalia Separator Gmbh | Three-phase Trennseparator |
SE535959C2 (en) * | 2010-01-29 | 2013-03-05 | Alfa Laval Corp Ab | Systems including centrifugal separator and method of checking the same |
EP2366457B1 (en) * | 2010-03-19 | 2013-03-06 | Alfa Laval Corporate AB | Device and method for monitoring and adjusting the radial position of an interface layer in a centrifugal separator |
US9400196B2 (en) * | 2013-11-12 | 2016-07-26 | Syncrude Canada Ltd. | Method of detecting and controlling E-line loss in a centrifuge |
EP3666384B1 (en) * | 2018-12-10 | 2021-08-18 | Alfa Laval Corporate AB | Centrifugal separator and method for eliminating air locks in a centrifugal separator |
US10654050B1 (en) | 2019-05-21 | 2020-05-19 | Empirical Innovations, Inc. | Centrifugal separators and separation methods employing multiple pistons and facilitating intermediate material ejection |
EP3782735B1 (en) | 2019-08-19 | 2022-03-30 | Alfa Laval Corporate AB | Centrifugal separation system and method of operating a centrifugal separator |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
NL280990A (en) * | 1961-09-29 | |||
NL286682A (en) * | 1961-12-22 | |||
US3261546A (en) * | 1962-10-29 | 1966-07-19 | Pfaudler Permutit Inc | Method for clarifying fats and oils |
NL128415C (en) * | 1963-01-26 | |||
DE1277757B (en) * | 1965-08-17 | 1968-09-12 | Westfalia Separator Ag | Device for triggering a signal or a control pulse depending on the filling of the sludge chamber of a centrifugal drum |
US3410479A (en) * | 1965-08-23 | 1968-11-12 | Alfa Laval Ab | Sludge level indicating device for centrifugal separators |
GB1139707A (en) * | 1966-11-14 | 1969-01-15 | Alfa Laval Ab | Improvements in sludge centrifuges |
DE1532767B2 (en) * | 1967-02-08 | 1971-06-03 | Westfaha Separator AG, 4740 Oelde | DEVICE FOR TRIGGERING A SIGNAL OR A CONTROL PULSE WHEN A PRE-DETERMINED LEVEL IS REACHED BY AT LEAST ONE SPRAYING MATERIAL THAT GIVES UP IN THE SLUDGE OF A SPIN DRUM |
SE322172B (en) * | 1967-10-31 | 1970-03-23 | Alfa Laval Ab |
-
1970
- 1970-12-07 SE SE16514/70D patent/SE345603B/xx unknown
-
1971
- 1971-11-23 SU SU711718637A patent/SU597323A3/en active
- 1971-11-26 IT IT31701/71A patent/IT941789B/en active
- 1971-11-30 FR FR7142921A patent/FR2117188A5/fr not_active Expired
- 1971-12-01 GB GB5575271A patent/GB1315250A/en not_active Expired
- 1971-12-03 US US00204625A patent/US3750940A/en not_active Expired - Lifetime
- 1971-12-06 DE DE19712160476 patent/DE2160476A1/en not_active Ceased
- 1971-12-07 JP JP9836471A patent/JPS5648217B1/ja active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2139121A (en) * | 1983-04-23 | 1984-11-07 | Westfalia Separator Ag | Centrifugal cleaning of used mineral oils |
GB2185425A (en) * | 1986-01-22 | 1987-07-22 | Westfalia Separator Ag | Regulating operation of a centrifuge |
GB2185425B (en) * | 1986-01-22 | 1989-10-25 | Westfalia Separator Ag | Process and apparatus for separating two liquid phases by means of a centrifuge |
Also Published As
Publication number | Publication date |
---|---|
SU597323A3 (en) | 1978-03-05 |
FR2117188A5 (en) | 1972-07-21 |
US3750940A (en) | 1973-08-07 |
DE2160476A1 (en) | 1972-06-15 |
SE345603B (en) | 1972-06-05 |
JPS5648217B1 (en) | 1981-11-14 |
IT941789B (en) | 1973-03-10 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed [section 19, patents act 1949] | ||
PCNP | Patent ceased through non-payment of renewal fee |