GB861897A - Process for the selective extraction of aromatic hydrocarbons from a mixture of both aromatic and non-aromatic hydrocarbons - Google Patents

Process for the selective extraction of aromatic hydrocarbons from a mixture of both aromatic and non-aromatic hydrocarbons

Info

Publication number
GB861897A
GB861897A GB24352/59A GB2435259A GB861897A GB 861897 A GB861897 A GB 861897A GB 24352/59 A GB24352/59 A GB 24352/59A GB 2435259 A GB2435259 A GB 2435259A GB 861897 A GB861897 A GB 861897A
Authority
GB
United Kingdom
Prior art keywords
solvent
separated
aromatic hydrocarbons
water
petroleum
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
GB24352/59A
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.)
Hokkaido Tanko Kisen KK
Original Assignee
Hokkaido Tanko Kisen KK
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 Hokkaido Tanko Kisen KK filed Critical Hokkaido Tanko Kisen KK
Publication of GB861897A publication Critical patent/GB861897A/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
    • C10G21/00Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents
    • C10G21/06Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents characterised by the solvent used
    • C10G21/12Organic compounds only
    • C10G21/16Oxygen-containing compounds

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)

Abstract

Aromatic hydrocarbons are separated from non-aromatic hydrocarbons by solvent extraction with a solvent comprising methyl alcohol, ethylene glycol in an amount of 40-80% by weight of the total solvent and optionally water. Aromatic hydrocarbons boiling in the range 75-280 DEG C. may be separated from non-aromatics boiling in the range 65-280 DEG C. The feed may be mixtures of specific hydrocarbons or oils such as crude petroleum, cracked petroleum, reformed petroleum, hydrocracked coal or carbonizated coal. Preferably, a tower having alternate mixing and settling zones is used, the solvent being introduced at the top, hydrocarbon feed at a mid-point and a reflux of separated aromatics at or near the bottom. Solvent is separated from the extract and raffinate by addition of water and then separated from water by distillation; up to 4% by weight of water may remain in the solvent. Extraction is effected at atmospheric pressure up to 40 DEG C. and 1-10 atmospheres up to 130 DEG C.ALSO:Aromatic hydrocarbons are separated from non-aromatic hydrocarbons by solvent extraction with a solvent comprising methyl alcohol, ethylene glycol in an amount of 40-80% by weight of the total solvent and optionally water. Aromatic hydrocarbons boiling in the range 75-280 DEG C. may be separated from nonaromatics boiling in the range 65-280 DEG C. The feed may be mixtures of specific hydrocarbons or oils such as crude petroleum, cracked petroleum, reformed petroleum, hydrocracked coal or carbonizated coal. Preferably, a tower having alternate mixing and settling zones is used, the solvent being introduced at the top, hydrocarbon feed at a mid-point and a reflux of separated aromatics at or near the bottom. Solvent is separated from the extract and raffinate by addition of water and then separated from water by distillation; up to 4% by weight of water may remain in the solvent. Extraction is effected at atmospheric pressure up to 40 DEG C. and 1-10 atmospheres up to 130 DEG C.
GB24352/59A 1958-07-18 1959-07-15 Process for the selective extraction of aromatic hydrocarbons from a mixture of both aromatic and non-aromatic hydrocarbons Expired GB861897A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP861897X 1958-07-18

Publications (1)

Publication Number Publication Date
GB861897A true GB861897A (en) 1961-03-01

Family

ID=13879807

Family Applications (1)

Application Number Title Priority Date Filing Date
GB24352/59A Expired GB861897A (en) 1958-07-18 1959-07-15 Process for the selective extraction of aromatic hydrocarbons from a mixture of both aromatic and non-aromatic hydrocarbons

Country Status (1)

Country Link
GB (1) GB861897A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2013177162A3 (en) * 2012-05-25 2014-01-16 Green Source Energy Llc Recovery of hydrocarbons from hydrocarbon-containing materials

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2013177162A3 (en) * 2012-05-25 2014-01-16 Green Source Energy Llc Recovery of hydrocarbons from hydrocarbon-containing materials
US9376629B2 (en) 2012-05-25 2016-06-28 Green Source Holdings Llc Recovery of hydrocarbons from hydrocarbon-containing materials

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