ES324827A1 - Procedure for the hydrogenating craqueo of a hydrocarboned oil. (Machine-translation by Google Translate, not legally binding) - Google Patents

Procedure for the hydrogenating craqueo of a hydrocarboned oil. (Machine-translation by Google Translate, not legally binding)

Info

Publication number
ES324827A1
ES324827A1 ES0324827A ES324827A ES324827A1 ES 324827 A1 ES324827 A1 ES 324827A1 ES 0324827 A ES0324827 A ES 0324827A ES 324827 A ES324827 A ES 324827A ES 324827 A1 ES324827 A1 ES 324827A1
Authority
ES
Spain
Prior art keywords
hydrogen
translation
hydrogenating
reaction zone
machine
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
ES0324827A
Other languages
Spanish (es)
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.)
Shell Internationale Research Maatschappij BV
Original Assignee
Shell Internationale Research Maatschappij BV
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 Shell Internationale Research Maatschappij BV filed Critical Shell Internationale Research Maatschappij BV
Publication of ES324827A1 publication Critical patent/ES324827A1/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
    • C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
    • C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
    • C10G65/10—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only cracking steps
    • 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
    • C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions

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

Abstract

Process for hydrogenating cracking a hydrocarbon oil, characterized in that the hydrocarbon oil is contacted, in the presence of hydrogen or a gas containing hydrogen, in a first reaction zone, with a catalyst containing a hydrogenation component and a cracking component that acts as an acid, under conditions such that the content of hydrocarbons boiling at not more than 525º C, in the hydrocarbon mixture leaving the first reaction zone is not less than 5% by weight nor greater than 65% by weight above the content in the hydrocarbon oil introduced in the first reaction zone, after which a hydrogen-containing gas and one or more hydrocarbon fractions having a final boiling point not greater than 525º C are separated from the reaction product, and at least a portion of the remaining part of the reaction product is then put in contact, in the presence of hydrogen or a gas containing hydrogen. Oxygen, in a second reaction zone, with a catalyst that also contains a hydrogenation component and a cracking component that acts as an acid. (Machine-translation by Google Translate, not legally binding)
ES0324827A 1965-03-31 1966-03-29 Procedure for the hydrogenating craqueo of a hydrocarboned oil. (Machine-translation by Google Translate, not legally binding) Expired ES324827A1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
NL656504066A NL144326B (en) 1965-03-31 1965-03-31 METHOD FOR HYDROGENATING CRACKING OF A HYDROCARBON OIL.

Publications (1)

Publication Number Publication Date
ES324827A1 true ES324827A1 (en) 1967-02-16

Family

ID=19792799

Family Applications (1)

Application Number Title Priority Date Filing Date
ES0324827A Expired ES324827A1 (en) 1965-03-31 1966-03-29 Procedure for the hydrogenating craqueo of a hydrocarboned oil. (Machine-translation by Google Translate, not legally binding)

Country Status (9)

Country Link
US (1) US3444071A (en)
BE (1) BE678609A (en)
CH (1) CH479687A (en)
DE (1) DE1276264B (en)
ES (1) ES324827A1 (en)
GB (1) GB1121443A (en)
NL (1) NL144326B (en)
NO (1) NO115222B (en)
SE (1) SE308936B (en)

Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3617484A (en) * 1968-11-29 1971-11-02 Sun Oil Co Increasing the v.i. of hydrocracked light lubes
BE754805A (en) * 1969-09-05 1971-02-15 Atlantic Richfield Co PERFECTED PROCESS FOR PREPARATION OF LUBRICATING MINERAL OIL FROM NEW RAW MATERIALS
US3617482A (en) * 1969-11-10 1971-11-02 Chevron Res Process for the production of lubricating oils
US3666657A (en) * 1970-11-16 1972-05-30 Sun Oil Co Pennsylvania Oil stabilizing sequential hydrocracking and hydrogenation treatment
US3992283A (en) * 1974-09-23 1976-11-16 Universal Oil Products Company Hydrocracking process for the maximization of an improved viscosity lube oil
US4419271A (en) * 1979-10-15 1983-12-06 Union Oil Company Of California Hydrocarbon conversion catalyst
US4743354A (en) * 1979-10-15 1988-05-10 Union Oil Company Of California Process for producing a product hydrocarbon having a reduced content of normal paraffins
US4743355A (en) * 1979-10-15 1988-05-10 Union Oil Company Of California Process for producing a high quality lube oil stock
US4592828A (en) * 1984-05-07 1986-06-03 Mobil Oil Corporation Process for upgrading petroleum residua
US5250588A (en) * 1990-01-16 1993-10-05 Ceram Sna Inc. Organic friction material composition for use to produce friction linings
US5358628A (en) * 1990-07-05 1994-10-25 Mobil Oil Corporation Production of high viscosity index lubricants

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3047490A (en) * 1958-11-04 1962-07-31 Phillips Petroleum Co Hydrocracking process
FR1327395A (en) * 1962-05-29 1963-05-17 California Research Corp Process for the hydrogenating cracking of petroleum hydrocarbons
US3242068A (en) * 1962-12-24 1966-03-22 Chevron Res Production of lubricating oil
US3308055A (en) * 1964-04-13 1967-03-07 Chevron Res Hydrocracking process producing lubricating oil

Also Published As

Publication number Publication date
DE1276264B (en) 1968-08-29
GB1121443A (en) 1968-07-24
BE678609A (en) 1966-09-29
US3444071A (en) 1969-05-13
NL144326B (en) 1974-12-16
CH479687A (en) 1969-10-15
SE308936B (en) 1969-03-03
NO115222B (en) 1968-09-02
NL6504066A (en) 1966-10-03

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