GB905809A - An improved method for the continuous selective hydrofining of crude petroleum in the liquid phase - Google Patents

An improved method for the continuous selective hydrofining of crude petroleum in the liquid phase

Info

Publication number
GB905809A
GB905809A GB34570/59A GB3457059A GB905809A GB 905809 A GB905809 A GB 905809A GB 34570/59 A GB34570/59 A GB 34570/59A GB 3457059 A GB3457059 A GB 3457059A GB 905809 A GB905809 A GB 905809A
Authority
GB
United Kingdom
Prior art keywords
crude petroleum
liquid phase
mixture
improved method
catalyst
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
GB34570/59A
Inventor
Clement Thonon
Jean Limido
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.)
IFP Energies Nouvelles IFPEN
Original Assignee
IFP Energies Nouvelles IFPEN
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 IFP Energies Nouvelles IFPEN filed Critical IFP Energies Nouvelles IFPEN
Publication of GB905809A publication Critical patent/GB905809A/en
Expired legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING 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
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING 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
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
    • C10G45/22—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing with hydrogen dissolved or suspended in the oil

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

Crude petroleum is hydrofined in the liquid phase by contacting a mixture of hydrogen and the crude oil with a catalyst selected from the oxides and sulphides of chromium, molybdenum, tungsten, iron, cobalt and nickel at 300 DEG -395 DEG C. and a pressure of 55 - 120 kg./cm2. Best results are obtained by employing the higher pressures in the quoted range with the lower temperatures. The mixture to be treated most suitably comprises a saturated solution of hydrogen in the crude petroleum, and the catalyst may be mounted in a fixed bed or suspended in the oil. The catalyst, which is preferably a mixture and/or compound of the oxides of molybdenum and cobalt, may be supported on silica, magnesium oxide, kieselguhr, activated carbon, or, most suitably, alumina, usually has a grain size of 0,1 - 10 mm., preferably 1 - 5 mm., when used in a fixed bed and a grain size of 0,05 - 0,5 mm. when used in solution.
GB34570/59A 1958-10-16 1959-10-12 An improved method for the continuous selective hydrofining of crude petroleum in the liquid phase Expired GB905809A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR776811A FR1313057A (en) 1958-10-16 1958-10-16 Continuous process for the selective hydrotreatment of crude oils in the liquid phase

Publications (1)

Publication Number Publication Date
GB905809A true GB905809A (en) 1962-09-12

Family

ID=8707747

Family Applications (1)

Application Number Title Priority Date Filing Date
GB34570/59A Expired GB905809A (en) 1958-10-16 1959-10-12 An improved method for the continuous selective hydrofining of crude petroleum in the liquid phase

Country Status (5)

Country Link
DE (1) DE1161373B (en)
ES (1) ES252619A1 (en)
FR (1) FR1313057A (en)
GB (1) GB905809A (en)
OA (1) OA01279A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
USRE29315E (en) * 1968-10-25 1977-07-19 Gulf Research & Development Company Asphaltene hydrodesulfurization with small catalyst particles utilizing a hydrogen quench for the reaction
USRE29314E (en) * 1968-10-25 1977-07-19 Gulf Research & Development Company Asphaltene hydrodesulfurization with small catalyst particles in a parallel reactor system
EP0534046A2 (en) * 1991-09-19 1993-03-31 Wolfdieter Klein Process for the treatment of contaminated liquid, liquefactable or solid hydrocarbons or hydrocarbon compounds
WO2003091363A1 (en) * 2002-04-23 2003-11-06 Bp Oil International Limited Purification process

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1950308A (en) * 1929-08-14 1934-03-06 Standard Ig Co Improved process for producing lubricants
US2073578A (en) * 1933-01-10 1937-03-09 Gwynn Marion Hayes Method of refining hydrocarbon distillates
US2145657A (en) * 1936-12-30 1939-01-31 Universal Oil Prod Co Process for the hydrogenation of hydrocarbon oils
FR977868A (en) * 1947-12-22 1951-04-06 Bataafsche Petroleum Catalytic refining process for distillable hydrocarbon oils
BE495784A (en) * 1948-01-06
US2608521A (en) * 1948-01-06 1952-08-26 Shell Dev Process for refining carbonaceous material
DE869198C (en) * 1950-05-21 1953-03-05 Basf Ag Process for purifying crude benzene
BE505693A (en) * 1950-09-07
DE930889C (en) * 1953-08-18 1955-07-28 Basf Ag Process for the production of gasoline from petroleum
DE954634C (en) * 1954-03-19 1956-12-20 Basf Ag Process for the catalytic pressure refining of low-boiling hydrocarbons
DE956539C (en) * 1954-09-04 1957-01-17 Metallgesellschaft Ag Process for refining hydrocarbons which are liquid under normal conditions by catalytic treatment with hydrogen or hydrogen-containing gases
DE1012718B (en) * 1955-09-01 1957-07-25 Metallgesellschaft Ag Process for the production of mixed diesel fuels

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
USRE29315E (en) * 1968-10-25 1977-07-19 Gulf Research & Development Company Asphaltene hydrodesulfurization with small catalyst particles utilizing a hydrogen quench for the reaction
USRE29314E (en) * 1968-10-25 1977-07-19 Gulf Research & Development Company Asphaltene hydrodesulfurization with small catalyst particles in a parallel reactor system
EP0534046A2 (en) * 1991-09-19 1993-03-31 Wolfdieter Klein Process for the treatment of contaminated liquid, liquefactable or solid hydrocarbons or hydrocarbon compounds
EP0534046A3 (en) * 1991-09-19 1993-04-14 Wolfdieter Klein Process for the treatment of contaminated liquid, liquefactable or solid hydrocarbons or hydrocarbon compounds
WO2003091363A1 (en) * 2002-04-23 2003-11-06 Bp Oil International Limited Purification process

Also Published As

Publication number Publication date
ES252619A1 (en) 1960-02-01
OA01279A (en) 1969-02-15
FR1313057A (en) 1962-12-28
DE1161373B (en) 1964-01-16

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