GB282738A - - Google Patents

Info

Publication number
GB282738A
GB282738A GB33397/27A GB3339727A GB282738A GB 282738 A GB282738 A GB 282738A GB 33397/27 A GB33397/27 A GB 33397/27A GB 3339727 A GB3339727 A GB 3339727A GB 282738 A GB282738 A GB 282738A
Authority
GB
United Kingdom
Prior art keywords
sulphur
oil
acid
sulphuric acid
reagent
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
GB33397/27A
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.)
AXTELL RESEARCH LABORATORIES Inc
Original Assignee
AXTELL RESEARCH LABORATORIES Inc
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 AXTELL RESEARCH LABORATORIES Inc filed Critical AXTELL RESEARCH LABORATORIES Inc
Publication of GB282738A publication Critical patent/GB282738A/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
    • C10G17/00Refining of hydrocarbon oils in the absence of hydrogen, with acids, acid-forming compounds or acid-containing liquids, e.g. acid sludge
    • C10G17/02Refining of hydrocarbon oils in the absence of hydrogen, with acids, acid-forming compounds or acid-containing liquids, e.g. acid sludge with acids or acid-containing liquids, e.g. acid sludge
    • C10G17/04Liquid-liquid treatment forming two immiscible phases
    • C10G17/06Liquid-liquid treatment forming two immiscible phases using acids derived from sulfur or acid sludge thereof

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

282,738. Axtell Research Laboratories, Inc., (Assignees of Axtell, F. C.). Dec. 27, 1926, [Convention date]. Mineral oils, purifying-The sulphur content of oils such as gasoline, kerosene, lubricating oils, or cracked distillates, is reduced by treatment with a reagent comprising sulphuric acid, preferably fuming, heated with excess of aromatic hydrocarbon preferably commercial benzene and its homologues at room temperature, whereby an acid sludge containing most of the sulphur is formed, and the aromatic and unsaturated content of the oil is unattacked. Concentrated sulphuric acid may be added to the reagent as required to react with the unsaturated portion. The oil is separated from the acid sludge, which may be largely freed from sulphur by adding water. The oil, preferably after treatment with a basic clay, which is then separated, is shaken with a strong aqueous alkali solutions. After separation, the oil is redistilled, and sulphur not separated in the acid sludge remains largely in the still. By treating an oil with an end boiling point of 225‹ C. with 12¢ lbs. of reagent per barrel, and blending with about 20 per cent of kerosene distillate and distilling wtih steam over caustic potash, the sulphur content is reduced from 0.68 per cent to 0.11 per cent. Commercial toluene and xylene may be added to or replace the benzene to raise the boiling point. The fuming sulphuric acid may contain enough sulphur trioxide to combine with any water formed on the formation of the benzene sulphonic acid. Crude distillates from cracking units may be first and immediately washed with caustic soda or sodium plumbite. The Specification as open to inspection under Sect. 91 (3) (a) comprises also the use of selenic acid in place of sulphuric acid. This subjectmatter does not appear in the Specification as accepted
GB33397/27A 1926-12-27 1927-12-09 Expired GB282738A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US282738TA 1926-12-27 1926-12-27

Publications (1)

Publication Number Publication Date
GB282738A true GB282738A (en) 1929-03-11

Family

ID=31945718

Family Applications (1)

Application Number Title Priority Date Filing Date
GB33397/27A Expired GB282738A (en) 1926-12-27 1927-12-09

Country Status (1)

Country Link
GB (1) GB282738A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2262942A (en) * 1990-05-30 1993-07-07 Tetsuo Aida Method of desulfurizing fuel oil

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2262942A (en) * 1990-05-30 1993-07-07 Tetsuo Aida Method of desulfurizing fuel oil

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