GB476610A - Fractional separation of crude hydrocarbon oil - Google Patents
Fractional separation of crude hydrocarbon oilInfo
- Publication number
- GB476610A GB476610A GB1700236A GB1700236A GB476610A GB 476610 A GB476610 A GB 476610A GB 1700236 A GB1700236 A GB 1700236A GB 1700236 A GB1700236 A GB 1700236A GB 476610 A GB476610 A GB 476610A
- Authority
- GB
- United Kingdom
- Prior art keywords
- carrier
- collected
- carriers
- fraction
- still
- 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
- C10G7/00—Distillation of hydrocarbon oils
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)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
<PICT:0476610/III/1> Crude hydrocarbon oils are separated into fractions by fractional distillation by adding to the crude oil in succession a number of carrier substances of known boiling point in order of magnitude of their boiling points, beginning with the lowest boiling-point substance, the series of carrier substances being selected so that each has a boiling point below the temperature at which the fraction to be collected would distil without the presence of the carrier substance and a vapour pressure at the desired distillation temperature sufficient to bring the total vapour pressure at that temperature of carrier substance and fraction to be collected up to the pressure in the still, distilling the mixture after the addition of each carrier and collecting the distillate until the boiling point of the carrier is reached and only the carrier comes over; whereafter the next carrier of the series is added and the procedure repeated. The carriers can be added in the vapour or liquid state and the distillation can be carried out under reduced pressure. The collected fractions can be separated from the carriers carried over therewith (1) mechanically when the fraction and carriers are immiscible, (2) by distillation when miscible. In an example the carriers used successively are hexane, decane, naphthalene, bromonaphthalene, and benzophenone. A still 1 provided with a stirrer 2 and a heating coil 3 is filled with the oil to be distilled. After air has been removed hexane from a container 5a is heated to boiling point in a coil 7 and then run into the still. The still is then heated until the lowest fraction and the carrier distil over, the distillate being condensed in the cooler 9 and collected in a receiver 10a. The remaining carriers are then added successively from the containers 5b, c, d, e, and the corresponding distillates collected in the receivers 10b, c, d, e, respectively.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB1700236A GB476610A (en) | 1936-06-18 | 1936-06-18 | Fractional separation of crude hydrocarbon oil |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB1700236A GB476610A (en) | 1936-06-18 | 1936-06-18 | Fractional separation of crude hydrocarbon oil |
Publications (1)
Publication Number | Publication Date |
---|---|
GB476610A true GB476610A (en) | 1937-12-13 |
Family
ID=10087474
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1700236A Expired GB476610A (en) | 1936-06-18 | 1936-06-18 | Fractional separation of crude hydrocarbon oil |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB476610A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2417355A (en) * | 1940-05-10 | 1947-03-11 | Aluminum Plant & Vessel Compan | Distillation of hydrocarbons with addition of acetone-methyl alcohol |
US2453205A (en) * | 1942-01-28 | 1948-11-09 | Anglo Iranian Oil Co Ltd | Controlled fractional distillation of petroleum |
US3167501A (en) * | 1961-07-18 | 1965-01-26 | Texaco Inc | Process for solvent refining hydrocarbon oils |
US3200065A (en) * | 1961-07-18 | 1965-08-10 | Texaco Inc | Hydrocarbon treatment process |
-
1936
- 1936-06-18 GB GB1700236A patent/GB476610A/en not_active Expired
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2417355A (en) * | 1940-05-10 | 1947-03-11 | Aluminum Plant & Vessel Compan | Distillation of hydrocarbons with addition of acetone-methyl alcohol |
US2453205A (en) * | 1942-01-28 | 1948-11-09 | Anglo Iranian Oil Co Ltd | Controlled fractional distillation of petroleum |
US3167501A (en) * | 1961-07-18 | 1965-01-26 | Texaco Inc | Process for solvent refining hydrocarbon oils |
US3200065A (en) * | 1961-07-18 | 1965-08-10 | Texaco Inc | Hydrocarbon treatment process |
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