GB827385A - Improved process for oxidising mercaptans or mercaptides to disulphides in a two-phase system consisting of a light hydrocarbon oil phase and an aqueous alkali metal hydroxide phase - Google Patents

Improved process for oxidising mercaptans or mercaptides to disulphides in a two-phase system consisting of a light hydrocarbon oil phase and an aqueous alkali metal hydroxide phase

Info

Publication number
GB827385A
GB827385A GB16593/56A GB1659356A GB827385A GB 827385 A GB827385 A GB 827385A GB 16593/56 A GB16593/56 A GB 16593/56A GB 1659356 A GB1659356 A GB 1659356A GB 827385 A GB827385 A GB 827385A
Authority
GB
United Kingdom
Prior art keywords
phenol
alkali metal
metal hydroxide
solution
water
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
GB16593/56A
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.)
Bataafsche Petroleum Maatschappij NV
Original Assignee
Bataafsche Petroleum Maatschappij NV
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 Bataafsche Petroleum Maatschappij NV filed Critical Bataafsche Petroleum Maatschappij NV
Publication of GB827385A publication Critical patent/GB827385A/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
    • C10G27/00Refining of hydrocarbon oils in the absence of hydrogen, by oxidation
    • C10G27/04Refining of hydrocarbon oils in the absence of hydrogen, by oxidation with oxygen or compounds generating oxygen
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07BGENERAL METHODS OF ORGANIC CHEMISTRY; APPARATUS THEREFOR
    • C07B45/00Formation or introduction of functional groups containing sulfur
    • C07B45/06Formation or introduction of functional groups containing sulfur of mercapto or sulfide groups

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

Light hydrocarbon oils having a boiling-point not above 370 DEG C and containing mercaptans, are purified by the oxidation process described in the parent Specification but employing, as the aqueous phase, a homogeneous aqueous solution of an alkali metal hydroxide and an alkali metal salt of a phenol containing at least 2 mols. per litre of free alkali metal hydroxide and not more than 54% by volume of water based on the total volumes of the components of the solution before they are mixed together, the aqueous solution being initially capable of co-existing in heterogeneous equilibrium with, and being initially saturated but not supersaturated with respect to, one or more solid compounds of the alkali metal hydroxide with either the phenol or the phenol and water. The hydrocarbon oils, phenols and general oxidation procedure are as described in the parent Specification. However, oxygen-yielding compounds such as ozone or a peroxide may be used in conjunction with the oxygen, for example as described in Specification 769,208. The compositions of the aqueous alkaline phenolate solutions only vary slightly from those described in the parent Specification and may be represented for the system in the graph 1 therein by the boundary lines DE and CD, but they allow use of smaller quantities of the solutions and regeneration of the latter is facilitated. Thus, the used alkaline solutions, which become diluted with water in use, may be regenerated by contact with a sufficient amount of a solid compound of the alkali metal hydroxide with the phenol or phenol and water, capable of coexisting in heterogeneous equilibrium with the original solution, whereby all or substantially all of the diluting water is drawn off. An example describes a continuous process for the sweetening of a gasoline using an aqueous KOH-potassium cresolate solution and the regeneration of the latter by means of anhydrous potassium cresolate; suitable apparatus is described.ALSO:Oil-soluble mercaptans or alkali-metal mercaptides derived therefrom are oxidized to disulphides by means of oxygen in the absence of an oxidation catalyst, the mercaptans or mercaptides being initially in a two-phase system, one phase of which is formed by a light hydrocarbon oil having a boiling-point or end boiling-point not exceeding 370 DEG C., and the other phase of which is formed by an aqueous solution of an alkali metal hydroxide and an alkali metal salt of a phenol as hereinafter defined, the two phases being brought into intimate contact with each other during the oxidation, the aqueous solution being a homogeneous solution containing at least 2 mols. per litre of free alkali metal hydroxide and not more than 54% by volume of water based on the total volumes of the components of the solution before they are mixed together, the aqueous solution also being initially capable of co-existing in heterogeneous equilibrium with, and initially being saturated but not supersaturated with respect to, one or more solid compounds of the alkali metal hydroxide with the phenol or of the alkali metal hydroxide with the phenol and water. The term "phenol" denotes phenol or a monohydric alkyl phenol containing a total of not more than 3 carbon atoms in the alkyl group or groups present and having no other substituents. The compositions of the aqueous solutions differ only slightly from those of the solutions used in the parent Specification, being representable for the system in graph 1 thereof by the boundary lines DE and CD, but they allow the use of smaller quantities of the alkaline solution and regeneration of the latter is facilitated. The oxidation is generally effected as described in the parent Specification. However, other oxygen-yielding compounds such as ozone or a peroxide may be used in conjunction with the oxygen; thus, a peroxide may be added as described in Specification 769,208. Regeneration of the aqueous alkaline solution, which becomes diluted with water in use, may be effected by contacting the used solution with a sufficient amount of a solid compound of the alkali metal hydroxide with the phenol or phenol and water, capable of co-existing in heterogeneous equilibrium with the original solution, whereby all or substantially all the diluting water is drawn off. The process is described with particular reference to mercaptan-containing gasolines and kerosenes, the sulphur remaining as disulphide in the treated oil. An example describes a continuous process for the oxidation of a mercaptan-containing gasoline using an aqueous KOH-potassium cresolate solution and the regeneration of the latter and suitable apparatus is illustrated.
GB16593/56A 1953-03-12 1956-05-29 Improved process for oxidising mercaptans or mercaptides to disulphides in a two-phase system consisting of a light hydrocarbon oil phase and an aqueous alkali metal hydroxide phase Expired GB827385A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
NL775015X 1953-03-12
NL197666 1955-05-31

Publications (1)

Publication Number Publication Date
GB827385A true GB827385A (en) 1960-02-03

Family

ID=26641593

Family Applications (3)

Application Number Title Priority Date Filing Date
GB7363/54A Expired GB775015A (en) 1953-03-12 1954-03-12 Process for oxidising mercaptans or mercaptides to disulphides in a two-phase system consisting of a light hydrocarbon oil phase and an aqueous alkali metal hydroxide phase
GB16593/56A Expired GB827385A (en) 1953-03-12 1956-05-29 Improved process for oxidising mercaptans or mercaptides to disulphides in a two-phase system consisting of a light hydrocarbon oil phase and an aqueous alkali metal hydroxide phase
GB16592/56A Expired GB827384A (en) 1953-03-12 1956-05-29 Improved process for oxidising mercaptans or mercaptides to disulphides in a two-phase system consisting of a light hydrocarbon oil phase and an aqueous alkali metal hydroxide phase

Family Applications Before (1)

Application Number Title Priority Date Filing Date
GB7363/54A Expired GB775015A (en) 1953-03-12 1954-03-12 Process for oxidising mercaptans or mercaptides to disulphides in a two-phase system consisting of a light hydrocarbon oil phase and an aqueous alkali metal hydroxide phase

Family Applications After (1)

Application Number Title Priority Date Filing Date
GB16592/56A Expired GB827384A (en) 1953-03-12 1956-05-29 Improved process for oxidising mercaptans or mercaptides to disulphides in a two-phase system consisting of a light hydrocarbon oil phase and an aqueous alkali metal hydroxide phase

Country Status (6)

Country Link
US (3) US2763594A (en)
BE (3) BE548193A (en)
DE (3) DE960918C (en)
FR (3) FR1097348A (en)
GB (3) GB775015A (en)
NL (3) NL80084C (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3107213A (en) * 1959-02-12 1963-10-15 Exxon Research Engineering Co Caustic treating process
US4513093A (en) * 1981-03-30 1985-04-23 Ashland Oil, Inc. Immobilization of vanadia deposited on sorbent materials during treatment of carbo-metallic oils
US7678263B2 (en) * 2006-01-30 2010-03-16 Conocophillips Company Gas stripping process for removal of sulfur-containing components from crude oil
JP6144352B2 (en) * 2012-11-09 2017-06-07 サウジ アラビアン オイル カンパニー Oxidative desulfurization process and system using gaseous oxidant enriched feed
US9643146B2 (en) 2013-11-29 2017-05-09 Uop Llc Unit for processing a liquid/gas phase mixture, mercaptan oxidation system including the same, and method of processing a liquid/gas phase mixture

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2015038A (en) * 1932-07-23 1935-09-17 Texas Co Process of sweetening petroleum hydrocarbons
US2164851A (en) * 1937-02-08 1939-07-04 Shell Dev Process of separating mercaptans contained in a hydrocarbon liquid
US2202039A (en) * 1938-06-25 1940-05-28 Shell Dev Process for the removal of mercaptans from hydrocarbon distillates
US2446507A (en) * 1945-01-26 1948-08-03 Socony Vacuum Oil Co Inc Method of removing mercaptans from a liquid mixture of hydrocarbons containing low-boiling and high-boiling mercaptans
US2556438A (en) * 1948-08-07 1951-06-12 Standard Oil Co Mercaptan extraction system
US2663674A (en) * 1950-03-17 1953-12-22 Standard Oil Co Refining sour hydrocarbon oils
BE510375A (en) * 1950-03-17
DE886947C (en) * 1951-11-28 1953-08-20 Bataafsche Petroleum Process for converting the mercaptans contained in petrol or kerosene into disulphides by oxidation with oxygen or an oxygen-containing gas

Also Published As

Publication number Publication date
BE548192A (en)
BE548193A (en)
DE1146217B (en) 1963-03-28
FR70001E (en) 1959-02-02
US2763594A (en) 1956-09-18
NL86366C (en)
GB775015A (en) 1957-05-15
US2893951A (en) 1959-07-07
DE1167470B (en) 1964-04-09
BE527146A (en)
DE960918C (en) 1957-03-28
FR70002E (en) 1959-02-02
US2862878A (en) 1958-12-02
NL86367C (en)
GB827384A (en) 1960-02-03
NL80084C (en)
FR1097348A (en) 1955-07-04

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