ES285937A1 - Continuous procedure for the hydrogenation in steam phase, of a distilled oil of hydrocarbons (Machine-translation by Google Translate, not legally binding) - Google Patents

Continuous procedure for the hydrogenation in steam phase, of a distilled oil of hydrocarbons (Machine-translation by Google Translate, not legally binding)

Info

Publication number
ES285937A1
ES285937A1 ES285937A ES285937A ES285937A1 ES 285937 A1 ES285937 A1 ES 285937A1 ES 285937 A ES285937 A ES 285937A ES 285937 A ES285937 A ES 285937A ES 285937 A1 ES285937 A1 ES 285937A1
Authority
ES
Spain
Prior art keywords
reaction
hydrogenation
translation
machine
legally binding
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
ES285937A
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.)
Gas Council
Original Assignee
Gas Council
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 Gas Council filed Critical Gas Council
Publication of ES285937A1 publication Critical patent/ES285937A1/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
    • C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • 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
    • C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/26—Fuel gas

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

Continuous process for the hydrogenation in the vapor phase of a hydrocarbon distillate oil, containing aliphatic components, characterized in that the oil vapor and a gas containing hydrogen are continuously introduced in the form of a jet at least through perforated elements, in a thermally insulated reaction chamber, in which the oil vapor reacts exothermically with hydrogen at a temperature comprised between 600º C and 800º C at a gauge pressure of at least 5 atmospheres; the gaseous products of the reaction are continuously removed from the reaction chamber; the reagents are introduced through perforated elements, at a high speed, and the arrangement is such that an appreciable mass of gas containing the two reactants and the reaction products is circulated continuously inside the chamber, and the reactants are preheated to such a degree that they maintain a reaction temperature within the limits mentioned, throughout the interior of the reaction chamber, except in the vicinity of the perforated elements. (Machine-translation by Google Translate, not legally binding)
ES285937A 1962-03-12 1963-03-11 Continuous procedure for the hydrogenation in steam phase, of a distilled oil of hydrocarbons (Machine-translation by Google Translate, not legally binding) Expired ES285937A1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB9478/62A GB1031717A (en) 1962-03-12 1962-03-12 Improvements in and relating to the hydrogenation of hydrocarbon oils

Publications (1)

Publication Number Publication Date
ES285937A1 true ES285937A1 (en) 1963-10-16

Family

ID=9872746

Family Applications (1)

Application Number Title Priority Date Filing Date
ES285937A Expired ES285937A1 (en) 1962-03-12 1963-03-11 Continuous procedure for the hydrogenation in steam phase, of a distilled oil of hydrocarbons (Machine-translation by Google Translate, not legally binding)

Country Status (9)

Country Link
JP (1) JPS509801B1 (en)
AT (1) AT248593B (en)
BE (1) BE629454A (en)
CH (1) CH467853A (en)
DE (1) DE1470701A1 (en)
DK (1) DK109102C (en)
ES (1) ES285937A1 (en)
FR (1) FR1350415A (en)
GB (1) GB1031717A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2121426A (en) * 1982-05-24 1983-12-21 British Gas Corp Hydrogenated carbonaceous solids
AU2989299A (en) * 1998-03-09 1999-09-27 Scott Specialty Gases, Inc. Method and apparatus for direct fluorination of carbon or sulfur compounds

Also Published As

Publication number Publication date
BE629454A (en)
JPS509801B1 (en) 1975-04-16
CH467853A (en) 1969-01-31
DE1470701A1 (en) 1969-06-19
AT248593B (en) 1966-08-10
DK109102C (en) 1968-03-18
FR1350415A (en) 1964-01-24
GB1031717A (en) 1966-06-02

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