GB704781A - Solvent refining of oils - Google Patents
Solvent refining of oilsInfo
- Publication number
- GB704781A GB704781A GB525351A GB525351A GB704781A GB 704781 A GB704781 A GB 704781A GB 525351 A GB525351 A GB 525351A GB 525351 A GB525351 A GB 525351A GB 704781 A GB704781 A GB 704781A
- Authority
- GB
- United Kingdom
- Prior art keywords
- extract
- solvent
- fractions
- extraction
- kerosene
- 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
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
In the solvent extraction of hydrocarbon oil fractions into relatively more paraffinic and more aromatic fractions the extract phase from one feed stock is employed as solvent for the extraction of a second fraction of overlapping or closely adjacent boiling range to the first. The second fraction is preferably the higher boiling. Conventional solvents and apparatus may be used to extract gasolene, kerosene, Diesel fuel, lubricating oils, aromatic cycle stock obtained in catalytic cracking, and fractions which have been subjected to hydrogenation, hydroforming, isomerization and the like. Light or burning fractions of increasing boiling point may be extracted using SO2 when the sulphur content of the aromatic extract increases from stage to stage while that of the raffinate decreases. Make up solvent such as SO2 or a modifying solvent may be added in the later stages. Thus, a gasoline extract is used for kerosene extraction, the kerosene extract + SO2 used for gas oil extraction, and this extract + benzol used to extract lubricating oil. Solvents recovered from the several extracts and raffinates are treated in a common recovery system. Specification 607,945 is referred to.
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
BE509744D BE509744A (en) | 1951-03-05 | ||
GB525351A GB704781A (en) | 1951-03-05 | 1951-03-05 | Solvent refining of oils |
FR1054976D FR1054976A (en) | 1951-03-05 | 1952-03-05 | Oil refining |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB525351A GB704781A (en) | 1951-03-05 | 1951-03-05 | Solvent refining of oils |
Publications (1)
Publication Number | Publication Date |
---|---|
GB704781A true GB704781A (en) | 1954-03-03 |
Family
ID=9792599
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB525351A Expired GB704781A (en) | 1951-03-05 | 1951-03-05 | Solvent refining of oils |
Country Status (3)
Country | Link |
---|---|
BE (1) | BE509744A (en) |
FR (1) | FR1054976A (en) |
GB (1) | GB704781A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3114783A (en) * | 1959-08-27 | 1963-12-17 | Exxon Research Engineering Co | Separation of aromatics from hydrocarbon streams |
EP0050381A1 (en) * | 1980-10-16 | 1982-04-28 | Shell Internationale Researchmaatschappij B.V. | Process for the simultaneous separation in aromatics and non-aromatics of a heavy hydrocarbon stream and a light hydrocarbon stream |
WO2013136169A1 (en) * | 2012-03-16 | 2013-09-19 | Bharat Petroleum Corporation Limited | Process for obtaining food grade hexane |
-
0
- BE BE509744D patent/BE509744A/xx unknown
-
1951
- 1951-03-05 GB GB525351A patent/GB704781A/en not_active Expired
-
1952
- 1952-03-05 FR FR1054976D patent/FR1054976A/en not_active Expired
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3114783A (en) * | 1959-08-27 | 1963-12-17 | Exxon Research Engineering Co | Separation of aromatics from hydrocarbon streams |
EP0050381A1 (en) * | 1980-10-16 | 1982-04-28 | Shell Internationale Researchmaatschappij B.V. | Process for the simultaneous separation in aromatics and non-aromatics of a heavy hydrocarbon stream and a light hydrocarbon stream |
EP0050381B1 (en) * | 1980-10-16 | 1984-07-25 | Shell Internationale Researchmaatschappij B.V. | Process for the simultaneous separation in aromatics and non-aromatics of a heavy hydrocarbon stream and a light hydrocarbon stream |
WO2013136169A1 (en) * | 2012-03-16 | 2013-09-19 | Bharat Petroleum Corporation Limited | Process for obtaining food grade hexane |
Also Published As
Publication number | Publication date |
---|---|
FR1054976A (en) | 1954-02-15 |
BE509744A (en) |
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