ES309633A1 - A procedure for the hydrogenation of a gasoline obtained from a thermal craqueo process. (Machine-translation by Google Translate, not legally binding) - Google Patents

A procedure for the hydrogenation of a gasoline obtained from a thermal craqueo process. (Machine-translation by Google Translate, not legally binding)

Info

Publication number
ES309633A1
ES309633A1 ES0309633A ES309633A ES309633A1 ES 309633 A1 ES309633 A1 ES 309633A1 ES 0309633 A ES0309633 A ES 0309633A ES 309633 A ES309633 A ES 309633A ES 309633 A1 ES309633 A1 ES 309633A1
Authority
ES
Spain
Prior art keywords
hydrogenation
translation
machine
legally binding
google translate
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
ES0309633A
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.)
BP PLC
Original Assignee
BP PLC
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 BP PLC filed Critical BP PLC
Priority to ES0309633A priority Critical patent/ES309633A1/en
Publication of ES309633A1 publication Critical patent/ES309633A1/en
Expired legal-status Critical Current

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  • Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

A process for the hydrogenation of a gasoline obtained from a thermal cracking process, operated at a temperature of at least 593 degrees centigrade and containing aromatics, monoolefins and unsaturated hydrocarbons that form gum, through a supported nickel catalyst, in the which nickel is present in greater proportion as elemental nickel, characterized by the fact that the pressure is 35.1 to 210.9 kilograms per square centimeter, the temperature is 50 to 200 degrees Celsius and the speed time is 0.1 to 5 volume per volume per hour, said pressure, temperature and velocity, being adjusted to give a hydrogen consumption of at least 300 cubic feet per Barrel, but lower than that at which the hydrogenation of aromatics occurs so that substantially all the unsaturated hydrocarbons that form gum and at least a proportion of the monoolefins are hydrogenated. (Machine-translation by Google Translate, not legally binding)
ES0309633A 1965-02-13 1965-02-13 A procedure for the hydrogenation of a gasoline obtained from a thermal craqueo process. (Machine-translation by Google Translate, not legally binding) Expired ES309633A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
ES0309633A ES309633A1 (en) 1965-02-13 1965-02-13 A procedure for the hydrogenation of a gasoline obtained from a thermal craqueo process. (Machine-translation by Google Translate, not legally binding)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
ES0309633A ES309633A1 (en) 1965-02-13 1965-02-13 A procedure for the hydrogenation of a gasoline obtained from a thermal craqueo process. (Machine-translation by Google Translate, not legally binding)

Publications (1)

Publication Number Publication Date
ES309633A1 true ES309633A1 (en) 1965-06-16

Family

ID=34501311

Family Applications (1)

Application Number Title Priority Date Filing Date
ES0309633A Expired ES309633A1 (en) 1965-02-13 1965-02-13 A procedure for the hydrogenation of a gasoline obtained from a thermal craqueo process. (Machine-translation by Google Translate, not legally binding)

Country Status (1)

Country Link
ES (1) ES309633A1 (en)

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