GB454690A - Improvements in or relating to processes for refining hydrocarbon oils - Google Patents

Improvements in or relating to processes for refining hydrocarbon oils

Info

Publication number
GB454690A
GB454690A GB25278/35A GB2527835A GB454690A GB 454690 A GB454690 A GB 454690A GB 25278/35 A GB25278/35 A GB 25278/35A GB 2527835 A GB2527835 A GB 2527835A GB 454690 A GB454690 A GB 454690A
Authority
GB
United Kingdom
Prior art keywords
raffinate
passes
solvent
acetone
oil
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
GB25278/35A
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.)
Texaco Development Corp
Original Assignee
Texaco Development Corp
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 Texaco Development Corp filed Critical Texaco Development Corp
Publication of GB454690A publication Critical patent/GB454690A/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
    • C10G21/02Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents with two or more solvents, which are introduced or withdrawn separately

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

In the extraction of mineral oils with a selective solvent for constituents of low viscosity-index (naphthenic components), to form a solvent-extract phase and a raffinate phase, the raffinate is freed from the solvent-extract phase retained therein by washing with a different solvent which completely dissolves this phase but has no solvent action on the raffinate, consisting of high viscosity-index (paraffinic) constituents. The distillation of the raffinate to remove solvent is thereby avoided. Lubricating - oil fractions which may contain wax are treated. Selective solvents specified are, furfural, nitrobenzene, aniline, benzaldehyde, benzophenone or dichlorethyl ether. The washing solvent may be low-boiling aliphatic alcohols or ketones such as ethyl alcohol, acetone or methyl ethyl ketone. A wax distillate is fed into a mixer 2 to which furfural containing some oil is admitted from a later stage. Extraction temperatures of 150 to 250 DEG F., are used The mixture passes to a separating vessel 4 from which the extract is drawn off into a still 34 to recover the furfural. The raffinate is led into a second mixer 6 together with a further amount of furfural and the mixture passes to a second separating vessel 9. The extract is removed and used in the first extraction stage. The raffinate passes to the bottom of a tower 11 and is washed in countercurrent with acetone which is admitted at the top. The acetone extract passes to a still to recover the acetone and the oil residue containing furfural passes to the mixer 2. The washed raffinate containing some acetone passes to a mixer 15 where a further amount of acetone and some benzol are added from the tank 16. The mixture is led to a chiller 18 where the temperature is lowered to 0 DEG F., or below. The resulting mixture containing precipitated wax is forced through a filter 20 and the de-waxed oil is led into a tank 21. The oil is freed from de-waxing solvents in a stripper 23 and the finished oil passes to a tank 26. A final treatment with filter clay may be used.
GB25278/35A 1934-09-12 1935-09-11 Improvements in or relating to processes for refining hydrocarbon oils Expired GB454690A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US454690XA 1934-09-12 1934-09-12

Publications (1)

Publication Number Publication Date
GB454690A true GB454690A (en) 1936-10-06

Family

ID=21938065

Family Applications (1)

Application Number Title Priority Date Filing Date
GB25278/35A Expired GB454690A (en) 1934-09-12 1935-09-11 Improvements in or relating to processes for refining hydrocarbon oils

Country Status (1)

Country Link
GB (1) GB454690A (en)

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