GB1182977A - Centrifugal Separators. - Google Patents
Centrifugal Separators.Info
- Publication number
- GB1182977A GB1182977A GB32314/67A GB3231467A GB1182977A GB 1182977 A GB1182977 A GB 1182977A GB 32314/67 A GB32314/67 A GB 32314/67A GB 3231467 A GB3231467 A GB 3231467A GB 1182977 A GB1182977 A GB 1182977A
- Authority
- GB
- United Kingdom
- Prior art keywords
- chamber
- oil
- water
- solids
- separated
- 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
- B04B15/00—Other accessories for centrifuges
-
- 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
- B04B15/00—Other accessories for centrifuges
- B04B15/08—Other accessories for centrifuges for ventilating or producing a vacuum in the centrifuge
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S494/00—Imperforate bowl: centrifugal separators
- Y10S494/901—Imperforate bowl: centrifugal separators involving mixture containing oil
Landscapes
- Centrifugal Separators (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
1,182,977. Centrifugal separator. WESTFALIA SEPARATOR A.G. 13 July, 1967 [15 July, 1966], No. 32314/67. Heading B2P. In a centrifuge for separating water and solids from oil, e.g. insulating oil, the separated oil is discharged under pressure from the centrifuge drum 1 by means of a skimmer 8 into a collecting chamber 12 which is sealed from a collecting chamber 5 for the separated water and solids and from a supply chamber 15 for the mixture to be separated. Separation takes place at a temperature of approximately 80C. The water and solids are periodically discharged from the sludge chamber 2 into the chamber 5 through valve-controlled openings 4. The oil passes inwardly of separating plates 3 and overflows via channels 6 into a skimming chamber 7 and thence through the skimmer 8, a channel 9, an annular chamber 10 and bores 11 into the chamber 12 in the form of a spray so that any water still retained in the oil is evaporated due to the release of pressure and may be discharged through the top part of a pipe 16 not filled completely with oil and leading to a container for the purified oil from which the vapourized water escapes. The chamber 12 may be connected to atmosphere through one or more passages 17 for the discharge of vapourized water. The chamber may also be connected via a fitting 18 to a vacuum pump in order to increase the evaporation effect.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEW0042010 | 1966-07-15 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1182977A true GB1182977A (en) | 1970-03-04 |
Family
ID=7603056
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB32314/67A Expired GB1182977A (en) | 1966-07-15 | 1967-07-13 | Centrifugal Separators. |
Country Status (4)
Country | Link |
---|---|
US (1) | US3460751A (en) |
DE (1) | DE1532763A1 (en) |
GB (1) | GB1182977A (en) |
SE (1) | SE343483B (en) |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5464536A (en) * | 1992-06-10 | 1995-11-07 | Charles W. Taggart | Apparatus for centrifugally separating a fluid mixture into its component parts |
US6719681B2 (en) | 1999-08-06 | 2004-04-13 | Econova, Inc. | Methods for centrifugally separating mixed components of a fluid stream |
US6607473B2 (en) | 1999-08-06 | 2003-08-19 | Econova Inc. | Methods for centrifugally separating mixed components of a fluid stream under a pressure differential |
US6346069B1 (en) | 1999-08-06 | 2002-02-12 | Separation Process Technology, Inc. | Centrifugal pressurized separators and methods of controlling same |
US7601858B2 (en) | 2004-08-17 | 2009-10-13 | Gs Cleantech Corporation | Method of processing ethanol byproducts and related subsystems |
US9108140B2 (en) | 2005-03-16 | 2015-08-18 | Gs Cleantech Corporation | Method and systems for washing ethanol production byproducts to improve oil recovery |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB429574A (en) * | 1934-02-26 | 1935-05-31 | Koefoed Hauberg Marstrand & Helweg As Titan | Improvements in or relating to centrifugal separators |
US3166503A (en) * | 1960-12-29 | 1965-01-19 | Separator Ab | Apparatus for centrifugal separation |
GB983690A (en) * | 1963-01-21 | 1965-02-17 | Separator Ab | Vacuum separator |
GB1091556A (en) * | 1963-09-13 | 1967-11-15 | Alfa Laval Co Ltd | Liquid purifying |
-
1966
- 1966-07-15 DE DE19661532763 patent/DE1532763A1/en active Pending
-
1967
- 1967-05-22 SE SE7595/67*A patent/SE343483B/xx unknown
- 1967-06-26 US US648788A patent/US3460751A/en not_active Expired - Lifetime
- 1967-07-13 GB GB32314/67A patent/GB1182977A/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
DE1532763A1 (en) | 1970-05-21 |
SE343483B (en) | 1972-03-13 |
US3460751A (en) | 1969-08-12 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed [section 19, patents act 1949] | ||
PLNP | Patent lapsed through nonpayment of renewal fees |