GB117615A - Improved Process and Apparatus for the Continuous Fractional Distillation of Petrols, Petroleums, Benzols and the like. - Google Patents
Improved Process and Apparatus for the Continuous Fractional Distillation of Petrols, Petroleums, Benzols and the like.Info
- Publication number
- GB117615A GB117615A GB1034118A GB1034118A GB117615A GB 117615 A GB117615 A GB 117615A GB 1034118 A GB1034118 A GB 1034118A GB 1034118 A GB1034118 A GB 1034118A GB 117615 A GB117615 A GB 117615A
- Authority
- GB
- United Kingdom
- Prior art keywords
- pipe
- column
- petrol
- led
- vapours
- 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
117,615. Barbet et fils et Cie, E. July 3, 1917, [Convention date]. Addition to 9088/14. Hydrocarbons, distilling.-In the continuous fractional distillation of petroleum, benzol, &c., the hydrocarbon is first dehydrated in an apparatus A, is then treated at atmospheric pressure in a plate column B for the separation of various grades of petrol, and is finally separated into white spirits, lighting petroleums, and a vaselinous residue by passage through apparatus D, E, F in succession. The apparatus D, E, F are under vacuum; the element E is heated by vapours generated in the element F, and the distillation in the element D is effected by the subjection of the hot liquid from the element B to the vacuum. The crude petroleum enters the dehydrating- column A by a pipe A' and the water with some of the petrol is evaporated by steam coils a<2>. The vapours are led to a condenser A<2>, and the petrol and water are separated in a testing-device a, the petrol being led to the boiler B' of the petrol-distilling column B. The dehydrated tar flows through a pipe b to the column B. Gasoline is obtained in a condenser B<2> receiving vapour from the column B and is led away by a pipe 1<1>. Petrol of various grades is collected from appropriate plates of the column B by means of pipes 2, 3, 4, 5. The hot petrol-free oil flows through a pipe b<2> to the column D and evaporates under the reduced pressure. Three grades of distillate are collected by pipes 6<5>, 7, 8. The residue flows by pipes d. c, e<2> to the elements E, F in succession. The elements E, F consist of boilers fitted with a froth-preventer and provided with heaters E<1>, F<1>. The heater F<1> is heated by steam, and the heater E' by vapours led from the element F by a pipe f. The fraction condensing in the heater E<1> is led away by a p pe 9<4>, and the uncondensed vapours are led by a pipe 9<5> to a cooler M. The vapours generated in the element E are led by, a pipe K to the column D to mix with those generated from the petroleum entering by the pipe d. The testing-devices of the apparatus D, E, F communicate with a vessel X which is evacuated by a pump Y which compresses the vapours inio a coil in a cooler L. Another coil in the coo'er L receives the vaselinous residue coming from the element F by a pipe f<1>.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR191409088X | 1913-04-12 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB117615A true GB117615A (en) | 1919-11-27 |
Family
ID=32526568
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB191409088D Expired GB191409088A (en) | 1913-04-12 | 1914-04-09 | Improved Process and Apparatus for the Continuous Fractional Distillation of Mixtures of Liquids having Different Boiling Points. |
GB1034118A Expired GB117615A (en) | 1913-04-12 | 1918-06-22 | Improved Process and Apparatus for the Continuous Fractional Distillation of Petrols, Petroleums, Benzols and the like. |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB191409088D Expired GB191409088A (en) | 1913-04-12 | 1914-04-09 | Improved Process and Apparatus for the Continuous Fractional Distillation of Mixtures of Liquids having Different Boiling Points. |
Country Status (2)
Country | Link |
---|---|
DE (1) | DE326418C (en) |
GB (2) | GB191409088A (en) |
-
1914
- 1914-04-07 DE DE1914326418D patent/DE326418C/de not_active Expired
- 1914-04-09 GB GB191409088D patent/GB191409088A/en not_active Expired
-
1918
- 1918-06-22 GB GB1034118A patent/GB117615A/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
DE326418C (en) | 1920-09-28 |
GB191409088A (en) | 1915-07-09 |
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