GB154558A - Improved method of distilling liquids, such as mineral oils, alcohol, and the like - Google Patents
Improved method of distilling liquids, such as mineral oils, alcohol, and the likeInfo
- Publication number
- GB154558A GB154558A GB15126/20A GB1512620A GB154558A GB 154558 A GB154558 A GB 154558A GB 15126/20 A GB15126/20 A GB 15126/20A GB 1512620 A GB1512620 A GB 1512620A GB 154558 A GB154558 A GB 154558A
- Authority
- GB
- United Kingdom
- Prior art keywords
- steam
- vapours
- generator
- pass
- column
- 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)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Fats And Perfumes (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
154,558. Granger, L., Mariller, C., and Soc. GÚnÚrale d'Evaporation (Procedes Prache et Bouillon), (formerly Soc. Anon d'Exploitation de ProcÚdÚs Evaporatoires, (SystÞme Prache et Bouillon)). Nov. 26, 1919, [Convention date]. Generating by indirect contact of heated gases.-The condensation of vapours in apparatus for distilling crude mineral oils, volatile hydrocarbons, alcoholic liquids &c. is utilized to generate steam which may be used for heating or power-producing. When distilling liquids with a boiling-point lower than water, steam is generated under reduced pressure and may be compressed. As applied to a continuous apparatus for distilling crude mineral oil, the oil is passed by a pipe 1, through a dephlegmator D, a water separator E and a preheater F to a column A in which petrol vapours are driven off and condensed in the dephlegmator D. The oil passes from the column A through a pipe 9, heater I and pipe 14 to a column B. The oil passes from the base of the column to a boiler C, the residues from which pass to the preheater F. Vapours pass from the column B by three pipes 11, 12, 13. The heavy vapours from ripe 13 are condensed in the heater I. The vapours from the pipe 12 pass to a steam-generator K of the type in which water is circulated rapidly through a number of tubes, either by heat action in inclined tubes or by a pump or impeller, so that steam will be generated when the temperature of the vapours is only slightly above the boiling point of water under the pressure maintained in the generator. The light vapours from the pipe 11 pass to a second steam-generator L of the same type. The steam from the generator K may be used in the heater G, the condensed water from which is returned to the generator K by a pump P. Residual steam and the steam from the generator L pass to a cylinder M, from which the steam may pass for the production of motive power, or may be compressed by a device T and used for heating purposes. The various oil condensates pass through a refrigerator J to the test glasses H. In non-continuous apparatus the vapours from a still are passed on their way to a condenser through a steam generator which is kept for example under a pressure of 6 atmospheres, so that steam is generated at about 150‹ C. by vapours at a temperature slightly above this, namely, about 163-165‹ C.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR154558X | 1919-11-26 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB154558A true GB154558A (en) | 1921-11-03 |
Family
ID=8876027
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB15126/20A Expired GB154558A (en) | 1919-11-26 | 1920-06-03 | Improved method of distilling liquids, such as mineral oils, alcohol, and the like |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB154558A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US9607756B2 (en) | 2011-07-08 | 2017-03-28 | E2V Technologies (Uk) Limited | Transformer for an inverter system and an inverter system comprising the transformer |
CN113332742A (en) * | 2021-06-30 | 2021-09-03 | 张婷娟 | Distillation type separation device for white mineral oil and xylene mixed solution |
-
1920
- 1920-06-03 GB GB15126/20A patent/GB154558A/en not_active Expired
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US9607756B2 (en) | 2011-07-08 | 2017-03-28 | E2V Technologies (Uk) Limited | Transformer for an inverter system and an inverter system comprising the transformer |
CN113332742A (en) * | 2021-06-30 | 2021-09-03 | 张婷娟 | Distillation type separation device for white mineral oil and xylene mixed solution |
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