GB763625A - Improvements in or relating to the purification of hydrocarbons - Google Patents

Improvements in or relating to the purification of hydrocarbons

Info

Publication number
GB763625A
GB763625A GB2643/54A GB264354A GB763625A GB 763625 A GB763625 A GB 763625A GB 2643/54 A GB2643/54 A GB 2643/54A GB 264354 A GB264354 A GB 264354A GB 763625 A GB763625 A GB 763625A
Authority
GB
United Kingdom
Prior art keywords
active carbon
acid
distillate
oxygen
column
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
GB2643/54A
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.)
Gelsenberg Benzin AG
Original Assignee
Gelsenberg Benzin AG
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 Gelsenberg Benzin AG filed Critical Gelsenberg Benzin AG
Publication of GB763625A publication Critical patent/GB763625A/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
    • C10G25/00Refining of hydrocarbon oils in the absence of hydrogen, with solid sorbents
    • C10G25/003Specific sorbent material, not covered by C10G25/02 or C10G25/03

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)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The mercaptan content of a hydrocarbon distillate, for example a gasoline, is reduced by leading the distillate through at least one column containing a layer of active carbon impregnated with an aqueous alkaline liquor and the used impregnated active carbon is subsequently regenerated by means of an oxygen-containing gas in the absence of steam. According to a modification of the process, the regeneration of the active carbon, instead of being effected subsequently, is effected continuously during the passage of the distillate through the column by adding air to the hydrocarbon distillate, either in the column or before the column. The alkaline liquor may be an aqueous solution of an alkali metal hydroxide, particularly sodium hydroxide, or of ammonium hydroxide, and the oxygen-containing gas may be air of oxygen. The alkaline liquor may contain organic or inorganic activators and a list of substances suitable for this purpose is given. Mercaptans in the hydrocarbon distillate are converted, by contact with the active carbon, to disulphides which remain dissolved in the distillate. The active carbon becomes contaminated with mercaptides and the regeneration with oxygen-containing gas effects removal of the mercaptides. The active carbon in time may become contaminated with phenolates and regeneration by steaming is then necessary. The hydrocarbon distillate, before contact with the active carbon, may be freed of hydrogen sulphide, for example by washing with aqueous sodium hydroxide solution, followed by water-washing and drying in a coalescer containing iron filings. In the examples, gasoline is sweetened by contact with active carbon impregnated with aqueous sodium or potassium hydroxide, air being introduced with the gasoline or used subsequently to regenerate the active carbon. Activators mentioned in the examples are methanol, glycol, dimethylamine, hydrochloride, diethanolamine, butyric acid, naphthenic acids, tartaric acid, acetaldehyde, acetone, grape sugar, phenol, m-cresol, petroleum phenols, alpha-naphthol, pyrocatechol, resorcinol, hydroquinone, pyrogallol, salicylic acid, resorcylic acid, gallic acid, tannin, p - aminophenol, N - benzyl - p - aminophenol, p - aminosalicylic acid, anthraquinone, alizarin, quinizarin, sodium salt of m - nitrobenzene sulphonic acid, picric acid, pyridine, hydrazine hydrate, hydroxides or sulphides of copper, ferric iron, chromium, manganese, lead, cobalt or nickel (formed in situ by the addition of a water-soluble salt of the metal and reaction between the salt and the alkaline liquor or sodium sulphide contained therein) and a mixture of ferric chloride and sodium potassium tartrate. Apparatus is described wherein the process employing air introduced with the hydrocarbon distillate is carried out in four towers, three being used in series and the fourth being out of action for steaming.
GB2643/54A 1953-02-06 1954-01-28 Improvements in or relating to the purification of hydrocarbons Expired GB763625A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE763625X 1953-02-06

Publications (1)

Publication Number Publication Date
GB763625A true GB763625A (en) 1956-12-12

Family

ID=6671370

Family Applications (1)

Application Number Title Priority Date Filing Date
GB2643/54A Expired GB763625A (en) 1953-02-06 1954-01-28 Improvements in or relating to the purification of hydrocarbons

Country Status (1)

Country Link
GB (1) GB763625A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001042392A2 (en) * 1999-12-13 2001-06-14 Ds2 Tech, Inc. Process for the demercaptanization of petroleum distillates
US6565741B2 (en) 1999-12-13 2003-05-20 William Wismann Process for desulfurization of petroleum distillates
EP1659163A1 (en) 2004-11-17 2006-05-24 Institut Français du Pétrole process for converting saturated sulfur compounds in a hydrocarbon fraction containing few or no olefins
CN103031141A (en) * 2011-09-29 2013-04-10 中国石油化工股份有限公司 Method for removing mercaptan in lightweight petroleum product
US9181501B2 (en) 2012-08-17 2015-11-10 Uop Llc Method and apparatus for removing H2S and moisture from fractionator overhead naphtha

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001042392A2 (en) * 1999-12-13 2001-06-14 Ds2 Tech, Inc. Process for the demercaptanization of petroleum distillates
WO2001042392A3 (en) * 1999-12-13 2002-03-14 Ds2 Tech Inc Process for the demercaptanization of petroleum distillates
US6485633B2 (en) 1999-12-13 2002-11-26 Ds2 Tech, Inc. Process for the demercaptanization of petroleum distillates
US6565741B2 (en) 1999-12-13 2003-05-20 William Wismann Process for desulfurization of petroleum distillates
EP1659163A1 (en) 2004-11-17 2006-05-24 Institut Français du Pétrole process for converting saturated sulfur compounds in a hydrocarbon fraction containing few or no olefins
CN103031141A (en) * 2011-09-29 2013-04-10 中国石油化工股份有限公司 Method for removing mercaptan in lightweight petroleum product
CN103031141B (en) * 2011-09-29 2015-11-25 中国石油化工股份有限公司 A kind of method removing mercaptan in oils
US9181501B2 (en) 2012-08-17 2015-11-10 Uop Llc Method and apparatus for removing H2S and moisture from fractionator overhead naphtha

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