GB672495A - Improvements in or relating to centrifugal separators - Google Patents
Improvements in or relating to centrifugal separatorsInfo
- Publication number
- GB672495A GB672495A GB16190/50A GB1619050A GB672495A GB 672495 A GB672495 A GB 672495A GB 16190/50 A GB16190/50 A GB 16190/50A GB 1619050 A GB1619050 A GB 1619050A GB 672495 A GB672495 A GB 672495A
- Authority
- GB
- United Kingdom
- Prior art keywords
- chamber
- bore
- centrifuge
- disc
- liquid
- 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
- B04B5/00—Other centrifuges
- B04B5/06—Centrifugal counter-current apparatus
Landscapes
- Extraction Or Liquid Replacement (AREA)
Abstract
672,495. Centrifugal machines. METALLGES. AKT.-GES. June 28, 1950 [July 8, 1949], No. 16190/50. Class 23 In a centrifuge having two or more chambers D, C in which liquids are brought into contact with one another, solids are separated from any of the liquids in a separate chamber E. Solids collected in the chamber E are periodically removed from' the centrifuge by spraying the chamber, or by removing the chamber and substituting a clean chamber. Alternatively the centrifuge may have two chambers E, one of which is in use while the other is being cleaned. Phenol is extracted by means of butyl acetate from a liquid supplied to the rotary centrifuge 1. The liquid traverses a bore 56 to the chamber E where the separated solids are collected. The clarified liquid is led from the chamber E by tubes 34, a passage 53 and a bore 60 to a mixing and distributing disc 48 in the chamber C. In passages in the disc the liquid is mixed with acetate containing phenol supplied from the chamber D by a bore 59. On leaving the disc the mixture is centrifugally separated in the chamber C, the acetate containing phenol being discharged from the centrifuge through a bore 58, and the extracted liquid being led to a further mixing and distributing disc 51 by a bore 61. The butyl acetate supplied to the centrifuge is led by a bore 57 to the disc 51. The mixture leaving the disc 51 is centrifugally separated in the chamber D, the completely extracted liquid being discharged from the centrifuge by a bore 55, and the acetate containing phenol being led by the bore 59 to the chamber C for further enrichment with phenol. Specification 414,558 is referred to.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE672495X | 1949-07-08 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB672495A true GB672495A (en) | 1952-05-21 |
Family
ID=6590743
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB16190/50A Expired GB672495A (en) | 1949-07-08 | 1950-06-28 | Improvements in or relating to centrifugal separators |
Country Status (2)
Country | Link |
---|---|
FR (1) | FR1015240A (en) |
GB (1) | GB672495A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2121325A (en) * | 1982-06-07 | 1983-12-21 | Fsp | Cleaning centrifuge |
-
1950
- 1950-03-28 FR FR1015240D patent/FR1015240A/en not_active Expired
- 1950-06-28 GB GB16190/50A patent/GB672495A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2121325A (en) * | 1982-06-07 | 1983-12-21 | Fsp | Cleaning centrifuge |
Also Published As
Publication number | Publication date |
---|---|
FR1015240A (en) | 1952-08-29 |
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