GB819846A - High temperature coking of residua - Google Patents

High temperature coking of residua

Info

Publication number
GB819846A
GB819846A GB32908/57A GB3290857A GB819846A GB 819846 A GB819846 A GB 819846A GB 32908/57 A GB32908/57 A GB 32908/57A GB 3290857 A GB3290857 A GB 3290857A GB 819846 A GB819846 A GB 819846A
Authority
GB
United Kingdom
Prior art keywords
gas oil
oil fraction
quench
light gas
fraction
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
GB32908/57A
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.)
ExxonMobil Technology and Engineering Co
Original Assignee
Exxon Research and Engineering Co
Esso Research and Engineering Co
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 Exxon Research and Engineering Co, Esso Research and Engineering Co filed Critical Exxon Research and Engineering Co
Publication of GB819846A publication Critical patent/GB819846A/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
    • C10G9/00Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G9/28Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid material
    • C10G9/30Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid material according to the "moving bed" method

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (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)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

Heavy oils are coked in a fluidized system by contacting the oils with fluidized particulate solids at above 1200 DEG F. to produce a vaporous product and a carbonaceous residue which is deposited on the particulate solids, separating the solids from the vaporous product, separating the vaporous product after quenching to obtain at least a naphtha product, a light gas oil fraction boiling below 650 DEG F., and a tar bottoms having an initial boiling point contiguous to the final boiling point of the light gas oil fraction, stripping from the tar bottoms an overhead fraction having a final boiling point below 800 DEG F. and condensing and combining the overhead fraction with a portion of the light gas oil fraction to obtain the liquid quench medium. In a typical example a feed comprising an 1100 DEG F. I.B.P. South Louisiana residuum is fed through a pipe into a transfer line zone, the temperature of which is 1400 DEG F. After approximately 0.75 sec. the reaction mixture is quenched by a liquid medium added through a line, the temperature after quench being 500 DEG F. The quench vapours are separated to obtain 26.8 per cent by weight of naphtha boiling below 430 DEG F., a gas oil fraction boiling from 430 DEG F. to 650 DEG F., and a heavy tar bottoms which is stripped with steam to remove a 650-700 DEG F. fraction which is combined with a larger quantity of the light gas oil fraction which is recycled to the quench point at a temperature of 240 DEG F. as a quench medium. The remainder of the light gas oil fraction amounting to 7.6 per cent by weight on the fresh feed, and of the stripped tar bottoms amounting to 30 per cent by weight are withdrawn as products.
GB32908/57A 1956-12-03 1957-10-22 High temperature coking of residua Expired GB819846A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US819846XA 1956-12-03 1956-12-03

Publications (1)

Publication Number Publication Date
GB819846A true GB819846A (en) 1959-09-09

Family

ID=22167657

Family Applications (1)

Application Number Title Priority Date Filing Date
GB32908/57A Expired GB819846A (en) 1956-12-03 1957-10-22 High temperature coking of residua

Country Status (1)

Country Link
GB (1) GB819846A (en)

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