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
Application number
GB1034118A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
E Barbet et Fils et Cie
Original Assignee
E Barbet et Fils et Cie
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by E Barbet et Fils et Cie filed Critical E Barbet et Fils et Cie
Publication of GB117615A publication Critical patent/GB117615A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G7/00Distillation 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>.
GB1034118A 1913-04-12 1918-06-22 Improved Process and Apparatus for the Continuous Fractional Distillation of Petrols, Petroleums, Benzols and the like. Expired GB117615A (en)

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)

Also Published As

Publication number Publication date
DE326418C (en) 1920-09-28
GB191409088A (en) 1915-07-09

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