GB374915A - Improvements in and connected with the separation of collcidal and other suspensionsfrom liquids - Google Patents
Improvements in and connected with the separation of collcidal and other suspensionsfrom liquidsInfo
- Publication number
- GB374915A GB374915A GB720531A GB720531A GB374915A GB 374915 A GB374915 A GB 374915A GB 720531 A GB720531 A GB 720531A GB 720531 A GB720531 A GB 720531A GB 374915 A GB374915 A GB 374915A
- Authority
- GB
- United Kingdom
- Prior art keywords
- water
- oil
- centrifuge
- impurities
- baffle
- 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
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M175/00—Working-up used lubricants to recover useful products ; Cleaning
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Centrifugal Separators (AREA)
Abstract
<PICT:0374915/III/1> <PICT:0374915/III/2> Used lubricating and similar oils are freed from suspended impurities, such as colloidal carbon, by forming a fine dispersion of water in the oil under pressure and separating the coagulated impurities. Used oil passes through an inlet 4 and is forced by a pump 5 into a vessel 7 in which it is heated to about 230 DEG F. The hot oil passes through a pipe 10 to a centrifuge 1 in which it is agitated with a small amount of hot water or steam admitted through pipes 15 and 11 from a heated tank 12. The mixture of water and oil is discharged through an outlet 1<1> into a time-lag tank 2 containing baffles, in which coagulation proceeds, preferably with the aid of an electric field. The mixture then passes into a centrifuge 3, to which a trickle of water is supplied through a pipe 16. Purified oil is discharged through an outlet 17, and the separated water and impurities pass through an outlet 18 into the tank 12, containing baffles. The supernatant layer of impurities is drawn off from a trough 19. The centrifuges 1, 3 may be combined in a unit in which the dispersion is formed at the centre of a rotating drum from which it is discharged against a pile of conical discs mounted therein. In a preferred form of the centrifuge 3, a preliminary separating space is provided adjacent the central inlet, by mounting an annular ring baffle 44, Fig. 3, between the flat bottom of the bowl 41 and the lowermost cone 42, so that the outer edge of the baffle extends into the water line, and the inner edge is just outside the oil line. The mixture of oil and water descends through the inlet 40 to the separating space between baffle 44 and cone 42. The water flows around the tubes 45, mounted in the baffle, to the water space surrounding the cones, and the oil forced downwards to the space 43 from which it rises through the tubes 45 to the oil level. The cones of the centrifuge may be alternately insulated and connected to a source of direct pulsating or alternating current. Specification 282,466, [Class 23, Centrifugal machines &c.], is referred to.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB720531A GB374915A (en) | 1931-03-09 | 1931-03-09 | Improvements in and connected with the separation of collcidal and other suspensionsfrom liquids |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB720531A GB374915A (en) | 1931-03-09 | 1931-03-09 | Improvements in and connected with the separation of collcidal and other suspensionsfrom liquids |
Publications (1)
Publication Number | Publication Date |
---|---|
GB374915A true GB374915A (en) | 1932-06-09 |
Family
ID=9828618
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB720531A Expired GB374915A (en) | 1931-03-09 | 1931-03-09 | Improvements in and connected with the separation of collcidal and other suspensionsfrom liquids |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB374915A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2743570A1 (en) * | 1996-01-17 | 1997-07-18 | Deutsch Richard Erwin | PROCESS FOR TREATING LUBRICATING OILS USED IN A WATER-BASED DISPERSE PHASE FOR THEIR RECYCLING |
US20150191661A1 (en) * | 2014-01-06 | 2015-07-09 | Aquifer Maintenance & Performance Systems, Inc. | Systems and methods for removing sulfer and halogens |
-
1931
- 1931-03-09 GB GB720531A patent/GB374915A/en not_active Expired
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2743570A1 (en) * | 1996-01-17 | 1997-07-18 | Deutsch Richard Erwin | PROCESS FOR TREATING LUBRICATING OILS USED IN A WATER-BASED DISPERSE PHASE FOR THEIR RECYCLING |
WO1997026314A1 (en) * | 1996-01-17 | 1997-07-24 | Richard Deutsch | Method for processing used lubricating oils in a dispersed aqueous phase for recycling |
US20150191661A1 (en) * | 2014-01-06 | 2015-07-09 | Aquifer Maintenance & Performance Systems, Inc. | Systems and methods for removing sulfer and halogens |
EP3092291A4 (en) * | 2014-01-06 | 2017-11-01 | Aquifer Maintenance & Performance Systems, Inc. | Systems and methods for removing sulfur and halogens |
US9840673B2 (en) * | 2014-01-06 | 2017-12-12 | Aquifer Maintenance & Performance Systems, Inc. | Systems and methods for removing sulfur and halogens |
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