GB362600A - An improved process for the purification of lubricating oils - Google Patents
An improved process for the purification of lubricating oilsInfo
- Publication number
- GB362600A GB362600A GB31569/30A GB3156930A GB362600A GB 362600 A GB362600 A GB 362600A GB 31569/30 A GB31569/30 A GB 31569/30A GB 3156930 A GB3156930 A GB 3156930A GB 362600 A GB362600 A GB 362600A
- Authority
- GB
- United Kingdom
- Prior art keywords
- phenol
- oil
- countercurrent
- lubricating oils
- 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
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G21/00—Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents
- C10G21/06—Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents characterised by the solvent used
- C10G21/12—Organic compounds only
- C10G21/16—Oxygen-containing compounds
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
<PICT:0362600/III/1> Lubricating oils are desulphurized and otherwise purified by undiluted liquid phenol at a temperature below that of complete miscibility. The use of 50-300 lb. of phenol to 100 lb. of oil at temperatures not higher than 250, 180, and 140 DEG F. in batch or countercurrent apparatus is specified. Phenol is separated from the extract and the treated oil by distillation. For example, 100-150 lb. of phenol and 100 lb. of oil from tanks 2, 1 are passed at 140 DEG F. or below through a countercurrent treater 3 to the phenol and oil store tanks 7, 6. Or the same proportions at the same temperature are passed through a series of agitators on the countercurrent principle, the mixture from any agitator being allowed to settle and the oil and phenol layers separated before passage to the next agitators. In the batch process the oil may be treated, separated, and retreated one or more times with fresh or previously used phenol.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US362600XA | 1929-10-29 | 1929-10-29 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB362600A true GB362600A (en) | 1931-12-10 |
Family
ID=21887598
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB31569/30A Expired GB362600A (en) | 1929-10-29 | 1930-10-21 | An improved process for the purification of lubricating oils |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB362600A (en) |
-
1930
- 1930-10-21 GB GB31569/30A patent/GB362600A/en not_active Expired
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