GB600801A - Improvements relating to the production of high grade aviation or motor fuels by fractional distillation - Google Patents

Improvements relating to the production of high grade aviation or motor fuels by fractional distillation

Info

Publication number
GB600801A
GB600801A GB117242A GB117242A GB600801A GB 600801 A GB600801 A GB 600801A GB 117242 A GB117242 A GB 117242A GB 117242 A GB117242 A GB 117242A GB 600801 A GB600801 A GB 600801A
Authority
GB
United Kingdom
Prior art keywords
column
pump
feedstock
tanks
controlled
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
GB117242A
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.)
Anglo Iranian Oil Co Ltd
Original Assignee
Anglo Iranian Oil Co Ltd
Filing date
Publication date
Application filed by Anglo Iranian Oil Co Ltd filed Critical Anglo Iranian Oil Co Ltd
Priority to US473608A priority Critical patent/US2453205A/en
Priority to NL122134A priority patent/NL67785C/xx
Priority to FR935749D priority patent/FR935749A/en
Publication of GB600801A publication Critical patent/GB600801A/en
Priority to NL254835A priority patent/NL122134C/xx
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
    • C10G7/02Stabilising gasoline by removing gases by fractioning
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D3/00Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/42Regulation; Control
    • B01D3/4211Regulation; Control of columns
    • B01D3/425Head-, bottom- and feed stream

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

<PICT:0600801/III/1> Closely cut petroleum fractions are obtained by fractionating a petroleum distillate in a column under conditions such that the ratio of the overhead or bottom products to the feed is controlled in accordance with the hydrocarbon content of the feed stock as established by analysis. In an example, the feed stock was analysed by determining its true boiling point curve using a laboratory batch column equivalent to at least 20 theoretical plates. The feedstock was found to have 12 per cent boiling below 72 DEG C. and distillation conditions were arranged so that with top and bottom column temperatures of 180 DEG F. and 280 DEG F. respectively, a reflux temperature of 125 DEG F., and an operating vapour velocity of 150,000 lbs. per hour, a reboil ratio (in lbs. per hour of vapours from reboiler and bottoms respectively) of 3.8-1 was maintained. A column e is provided with a reboiler m and an off-take pump o, operation of which is controlled by a level controller n to maintain a constant level in the bottom of the column. Overhead is withdrawn through condenser f and the overhead product is collected in tank g part being recirculated as reflux by the pump k, while the remainder is withdrawn by pump l; operation of pump k is controlled by controller h in tank g. The feedstock is supplied through two or more tanks, so that when the feedstock in one of the tanks is being analysed supply can be continued from one of the other tanks. Specification 600,551 is referred to.
GB117242A 1942-01-28 1942-01-28 Improvements relating to the production of high grade aviation or motor fuels by fractional distillation Expired GB600801A (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
US473608A US2453205A (en) 1942-01-28 1943-01-26 Controlled fractional distillation of petroleum
NL122134A NL67785C (en) 1942-01-28 1945-11-24
FR935749D FR935749A (en) 1942-01-28 1946-11-05 Continuous distillation process for the production of high quality aviation or motor fuels
NL254835A NL122134C (en) 1942-01-28 1960-08-12

Publications (1)

Publication Number Publication Date
GB600801A true GB600801A (en) 1948-04-20

Family

ID=1626701

Family Applications (1)

Application Number Title Priority Date Filing Date
GB117242A Expired GB600801A (en) 1942-01-28 1942-01-28 Improvements relating to the production of high grade aviation or motor fuels by fractional distillation

Country Status (1)

Country Link
GB (1) GB600801A (en)

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