GB943239A - Improvements relating to the treatment of hydrocarbon fractions - Google Patents

Improvements relating to the treatment of hydrocarbon fractions

Info

Publication number
GB943239A
GB943239A GB824861A GB824861A GB943239A GB 943239 A GB943239 A GB 943239A GB 824861 A GB824861 A GB 824861A GB 824861 A GB824861 A GB 824861A GB 943239 A GB943239 A GB 943239A
Authority
GB
United Kingdom
Prior art keywords
catalyst
halogen
hydrogen
temperature
compounds
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
GB824861A
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.)
DONALD RICHARD IRVING
BP PLC
Original Assignee
DONALD RICHARD IRVING
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 DONALD RICHARD IRVING, BP PLC filed Critical DONALD RICHARD IRVING
Priority to GB824861A priority Critical patent/GB943239A/en
Publication of GB943239A publication Critical patent/GB943239A/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
    • C10G45/58Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins
    • C10G45/60Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins characterised by the catalyst used
    • C10G45/62Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins characterised by the catalyst used containing platinum group metals or compounds thereof
    • 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
    • C10G65/00Treatment of hydrocarbon oils by two or more hydrotreatment processes only
    • C10G65/02Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
    • C10G65/04Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps
    • C10G65/043Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps at least one step being a change in the structural skeleton
    • 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
    • C10G67/00Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only
    • C10G67/02Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only
    • C10G67/04Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only including solvent extraction as the refining step in the absence of hydrogen

Abstract

Hydrocarbon fractions boiling above 150 DEG C., e.g. heavy gas oils, are treated to reduce their content of aromatic compounds and nitrogen compounds, and are then contacted in the presence of hydrogen with a platinum group metal on a refractory oxide support at a temperature of at least 600 DEG F. and a pressure of at least 100 p.s.i.g., the temperature and space velocity being correlated to give a product boiling above 150 DEG C. having a pour point at least 5 DEG F. lower than the pour point of the feedstock. The cloud point and freezing point of the fractions may also be lowered. Suitable hydrogenation conditions are: .Temperature.600-950 DEG F .Space velocity.0.1-8 v/v/hr .Pressure.100-1500 p.s.i.g .Hydrogen :hydrocarbon mole ratio.1:1- .20 : 1.. The process may be operated with or without a net hydrogen consumption. The catalyst support may be one or more of the oxides of metals of Groups II, III and IV, preferably alumina containing 5-25% wt. silica. A minor proportion of one or more compounds of non-metallic elements of Groups III, IV and V, e.g. boron or phosphorus, may be present. The catalyst may also contain halogen, e.g. fluorine or chlorine. Further, halogen may be added to the reaction zone to increase the activity of the catalyst, either as such or in the form of a compound which decomposes to the halogen under the reaction conditions, e.g. as hydrogen halides or as halogen derivatives of aliphatic hydrocarbon having 1-4 carbon atoms. The reduction of the content of aromatics and nitrogen compounds may be effected by destroying them by catalytic hydrogenation, e.g. with a cobalt molybdate-alumina or similar catalyst. Alternatively they may be removed by a method in which they may later be recovered, for example by solvent extraction, e.g. with furfural, sulphur dioxide, or a glycol, washing with sulphuric acid, urea adduction, or adsorption, for example on silica gel or a 5<\>rA or 13<\>rA molecular sieve. Specifications 928,460, 942,237 and 943,938 are referred to.
GB824861A 1961-03-07 1961-03-07 Improvements relating to the treatment of hydrocarbon fractions Expired GB943239A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB824861A GB943239A (en) 1961-03-07 1961-03-07 Improvements relating to the treatment of hydrocarbon fractions

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB824861A GB943239A (en) 1961-03-07 1961-03-07 Improvements relating to the treatment of hydrocarbon fractions

Publications (1)

Publication Number Publication Date
GB943239A true GB943239A (en) 1963-12-04

Family

ID=9848855

Family Applications (1)

Application Number Title Priority Date Filing Date
GB824861A Expired GB943239A (en) 1961-03-07 1961-03-07 Improvements relating to the treatment of hydrocarbon fractions

Country Status (1)

Country Link
GB (1) GB943239A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0518294A1 (en) * 1991-06-11 1992-12-16 Kawasaki Steel Corporation Method for refining methylnaphthalene containing oil
EP0528384A2 (en) * 1991-08-16 1993-02-24 Kawasaki Steel Corporation Process for preparing 2-methylnaphthalene
EP0621334A1 (en) * 1993-04-23 1994-10-26 Institut Français du Pétrole Process for producing a fuel by extraction and hydrotreatment of a hydrocarboneous feed and produced gasoil

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0518294A1 (en) * 1991-06-11 1992-12-16 Kawasaki Steel Corporation Method for refining methylnaphthalene containing oil
US5284552A (en) * 1991-06-11 1994-02-08 Kawasaki Steel Corporation Method for refining methylnaphthalene-containing oil
EP0528384A2 (en) * 1991-08-16 1993-02-24 Kawasaki Steel Corporation Process for preparing 2-methylnaphthalene
EP0528384A3 (en) * 1991-08-16 1993-04-21 Kawasaki Steel Corporation Process for preparing 2-methylnaphthalene
EP0621334A1 (en) * 1993-04-23 1994-10-26 Institut Français du Pétrole Process for producing a fuel by extraction and hydrotreatment of a hydrocarboneous feed and produced gasoil
FR2704232A1 (en) * 1993-04-23 1994-10-28 Inst Francais Du Petrole Process for improving the qualities of a hydrocarbon feedstock by extraction and hydrodesulfurization and the diesel fuel obtained.
US5527448A (en) * 1993-04-23 1996-06-18 Institut Francais Du Petrole Process for obtaining a fuel through extraction and hydrotreatment of a hydrocarbon charge, and the gas oil obtained
US5718820A (en) * 1993-04-23 1998-02-17 Institut Francais Du Petrole Petroleum fuel base

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