GB196306A - Process of, and means for, distilling and fractionating hydrocarbon oils - Google Patents
Process of, and means for, distilling and fractionating hydrocarbon oilsInfo
- Publication number
- GB196306A GB196306A GB2750121A GB2750121A GB196306A GB 196306 A GB196306 A GB 196306A GB 2750121 A GB2750121 A GB 2750121A GB 2750121 A GB2750121 A GB 2750121A GB 196306 A GB196306 A GB 196306A
- Authority
- GB
- United Kingdom
- Prior art keywords
- heated
- chamber
- pass
- oil
- distilling
- 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)
Abstract
196,306. French, E. H. Oct. 17, 1921. Hydrocarbons, distilling; spray evaporators; separate heater and evaporator apparatus.-Hydrocarbon oils are heated by passage through a coil C, to a temperature below the average boiling point of the fraction to be removed and are sprayed by natural gas, steam, or the uncondensed gases obtained in the process, heated in a coil L<2>, into a separating chamber E which may be heated and under reduced pressure. The unvolatilized oil falls on to an inclined bottom 6 and is led by a pipe 8 to a chamber F. The vapours pass through a heated scrubbing-tower G from which condensates pass to the chamber F, to tubular condensers I, I<1>, I<2>, the later ones of which mav be fitted with jackets for circulation of cooling water, and a scrubbing tower G<1>. Uncondensed gases are withdrawn by a pump K and are passed to a storage tank L, or to a tank L<1> from which they pass to the heater L<2>. The residual oil from the chamber F mav be passed through a similar apparatus, in which higher temperatures are used, When a light fraction is to be separated, the oil may be sprayed without preliminary heating, the separating- chamber E only being heated. Reference has been directed by the Comptroller to Specifications 13089/91, 7108/97, and 107,502.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2750121A GB196306A (en) | 1921-10-17 | 1921-10-17 | Process of, and means for, distilling and fractionating hydrocarbon oils |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2750121A GB196306A (en) | 1921-10-17 | 1921-10-17 | Process of, and means for, distilling and fractionating hydrocarbon oils |
Publications (1)
Publication Number | Publication Date |
---|---|
GB196306A true GB196306A (en) | 1923-04-17 |
Family
ID=10260592
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2750121A Expired GB196306A (en) | 1921-10-17 | 1921-10-17 | Process of, and means for, distilling and fractionating hydrocarbon oils |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB196306A (en) |
-
1921
- 1921-10-17 GB GB2750121A patent/GB196306A/en not_active Expired
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