GB427632A - Process for the stabilisation of liquid hydrocarbons especially motor fuels - Google Patents

Process for the stabilisation of liquid hydrocarbons especially motor fuels

Info

Publication number
GB427632A
GB427632A GB2891133A GB2891133A GB427632A GB 427632 A GB427632 A GB 427632A GB 2891133 A GB2891133 A GB 2891133A GB 2891133 A GB2891133 A GB 2891133A GB 427632 A GB427632 A GB 427632A
Authority
GB
United Kingdom
Prior art keywords
catalysts
employed
benzines
hydrogen
free hydrogen
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
GB2891133A
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.)
INT HYDROGENATION PATENTS CO
International Hydrogenation Patents Co Ltd
Original Assignee
INT HYDROGENATION PATENTS CO
International Hydrogenation Patents Co Ltd
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 INT HYDROGENATION PATENTS CO, International Hydrogenation Patents Co Ltd filed Critical INT HYDROGENATION PATENTS CO
Priority to GB2891133A priority Critical patent/GB427632A/en
Publication of GB427632A publication Critical patent/GB427632A/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
    • C10G45/00Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/32Selective hydrogenation of the diolefin or acetylene compounds
    • 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
    • C10G2400/00Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/02Gasoline

Abstract

Relates to the gum stabilization of hydrocarbon products, particularly motor fuels, without substantial reduction of their octane number; and consists in treating such hydrocarbon products in the vapour phase with gases consisting of or containing free hydrogen, while in contact with hydrogenating catalysts resistant to poisoning by sulphur, at elevated temperature and with a partial pressure of oil vapour between 40 and 80 per cent, the time of contact being not more than 50 seconds. The partial pressure of free hydrogen is, preferably, at least 20 per cent. With strongly hydrogenating catalysts pressures below 30, e.g. 10 atmospheres may be employed, with less active catalysts, pressures of 50, 100, 200 atmospheres or more may be used. Temperatures of at least 275 DEG C., e.g. 300--400 DEG C., are employed; but for initial materials consisting substantially of aliphatic hydrocarbons lower temperatures, e.g. 200--275 DEG C., may be desirable. The materials may be pretreated with adsorbents, e.g. bleaching or Fuller's earth, diatomaceous earth, silica gel, active carbon or coke. Suitable catalysts are heavy metals of the sixth group of the periodic system, especially molybdenum and tungsten; but chromium and uranium and their compounds or sulphur-immune compounds of tin, titanium, vanadium, rhenium, manganese, zinc, cadmium, aluminium, iron, nickel or cobalt, e.g. sulphides may be employed. The catalysts may be deposited on carriers. Gases containing free hydrogen may comprise mixtures of hydrogen with nitrogen, carbon dioxide, hydrogen sulphide, water vapour, methane &c., or water gas. As initial materials, benzines derived from cracking, low temperature carbonization or destructive hydrogenation operations may be employed; also benzol, toluol, kerosene and neutral portions of coal tar oils having a boiling range of benzines, or of safety aviation or marine fuels. Examples are given of the treatment of gasoline and benzines using tungsten disulphide or molybdenum sulphide as catalyst. Specifications 22147/14, 300,900, [both in Class 91], and 379,335 are referred to.
GB2891133A 1933-10-19 1933-10-19 Process for the stabilisation of liquid hydrocarbons especially motor fuels Expired GB427632A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB2891133A GB427632A (en) 1933-10-19 1933-10-19 Process for the stabilisation of liquid hydrocarbons especially motor fuels

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB2891133A GB427632A (en) 1933-10-19 1933-10-19 Process for the stabilisation of liquid hydrocarbons especially motor fuels

Publications (1)

Publication Number Publication Date
GB427632A true GB427632A (en) 1935-04-23

Family

ID=10283177

Family Applications (1)

Application Number Title Priority Date Filing Date
GB2891133A Expired GB427632A (en) 1933-10-19 1933-10-19 Process for the stabilisation of liquid hydrocarbons especially motor fuels

Country Status (1)

Country Link
GB (1) GB427632A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2934574A (en) * 1957-01-11 1960-04-26 Tidewater Oil Company Selective hydrogenation of butadiene in admixture with butenes with cobalt molybdateas catalyst
US3113983A (en) * 1959-04-07 1963-12-10 Air Prod & Chem Selective hydrogenation of diolefins
CN108300509A (en) * 2017-01-12 2018-07-20 中国石油化工股份有限公司 A method of producing bunker fuel oil

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2934574A (en) * 1957-01-11 1960-04-26 Tidewater Oil Company Selective hydrogenation of butadiene in admixture with butenes with cobalt molybdateas catalyst
US3113983A (en) * 1959-04-07 1963-12-10 Air Prod & Chem Selective hydrogenation of diolefins
CN108300509A (en) * 2017-01-12 2018-07-20 中国石油化工股份有限公司 A method of producing bunker fuel oil
CN108300509B (en) * 2017-01-12 2020-04-28 中国石油化工股份有限公司 Method for producing bunker fuel oil

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