GB345738A - Improvements in the purification of mineral oils, tars, their distillation products and the like - Google Patents

Improvements in the purification of mineral oils, tars, their distillation products and the like

Info

Publication number
GB345738A
GB345738A GB241030A GB241030A GB345738A GB 345738 A GB345738 A GB 345738A GB 241030 A GB241030 A GB 241030A GB 241030 A GB241030 A GB 241030A GB 345738 A GB345738 A GB 345738A
Authority
GB
United Kingdom
Prior art keywords
hydrogen
earth
catalysts
oils
sulphides
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
GB241030A
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.)
IG Farbenindustrie AG
Original Assignee
IG Farbenindustrie AG
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 IG Farbenindustrie AG filed Critical IG Farbenindustrie AG
Priority to GB241030A priority Critical patent/GB345738A/en
Publication of GB345738A publication Critical patent/GB345738A/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
    • C10G45/02Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
    • C10G45/24Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing with hydrogen-generating compounds
    • C10G45/28Organic compounds; Autofining
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10CWORKING-UP PITCH, ASPHALT, BITUMEN, TAR; PYROLIGNEOUS ACID
    • C10C1/00Working-up tar
    • C10C1/20Refining by chemical means inorganic or organic 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
    • C10G45/00Refining of hydrocarbon oils using hydrogen or hydrogen-generating 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
    • C10G45/00Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/02Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
    • 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

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)
  • Materials Engineering (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)

Abstract

Mineral oils, tars, synthetic oils, and the like are refined by first removing, by polymerization, adsorption, or decomposition, those constituents which resinify or decompose when heated to 400 DEG C. in the presence of hydrogen, and then treating the resulting products with hydrogen at elevated temperatures in the presence of catalysts immune from poisoning by sulphur, if desired under pressure, so as to convert unsaturated compounds and compounds containing sulphur, oxygen, nitrogen, or halogens into hydrocarbons without substantial cracking. The removal of the injurious constituents in the first stage may be effected by stirring with dilute or weak acids such as 40 per cent sulphuric acid, or acetic, oxalic, or malonic acid; or by the addition of polymerizing catalysts such as sulphur, potassium hydrosulphide, zinc chloride, or aluminium chloride; or by heating in the liquid or vapour state under normal or elevated pressure with bleaching earth, silica gel, pumice, bauxite, and the like. In the latter treatment in the vapour state, gases such as hydrogen, water vapour, or air may be added. High boiling materials are preferably diluted with middle oils which are distilled off later. The second stage treatment with hydrogen is preferably carried out at 200-450 DEG C. with catalysts containing oxides or sulphides of the metals of groups 2-7, preferably in conjunction with metals of group 8 or with heavy metals of groups 1 and 2, or the oxides and sulphides thereof. The catalysts are preferably deposited on charcoal, Florida earth, silica gel and the like. In examples (1) benzol is passed with hydrogen over Florida earth at 250 DEG C., and then over nickel oxide and tungsten oxide on active carbon at 300 DEG C.; (2) solvent benzol of B.P. 140-200 DEG C. is passed with hydrogen at 200 atmospheres and 250 DEG C. through bleaching earth, and is then passed at the same pressure at 350 DEG C. over nickel sulphide and chromium oxide on fuller's earth; (3) a coal-tar middle oil of B.P. 120-350 DEG C. is washed with 40 per cent sulphuric acid, distilled, and treated in the liquid phase with hydrogen at 200 atmospheres and 350 DEG C. with a catalyst of cobalt and molybdenum sulphides, with or without zinc oxide, on Florida earth. Specifications 249,309, [Class 91, Oils &c.], 267,165, 325,862, and 332,336, [all in Class 32, Distilling &c.], are referred to.
GB241030A 1930-01-23 1930-01-23 Improvements in the purification of mineral oils, tars, their distillation products and the like Expired GB345738A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB241030A GB345738A (en) 1930-01-23 1930-01-23 Improvements in the purification of mineral oils, tars, their distillation products and the like

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB241030A GB345738A (en) 1930-01-23 1930-01-23 Improvements in the purification of mineral oils, tars, their distillation products and the like

Publications (1)

Publication Number Publication Date
GB345738A true GB345738A (en) 1931-04-02

Family

ID=9739055

Family Applications (1)

Application Number Title Priority Date Filing Date
GB241030A Expired GB345738A (en) 1930-01-23 1930-01-23 Improvements in the purification of mineral oils, tars, their distillation products and the like

Country Status (1)

Country Link
GB (1) GB345738A (en)

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2542970A (en) * 1946-06-15 1951-02-27 Standard Oil Dev Co Refining of cracked naphthas by selective hydrogenation
US2636843A (en) * 1950-10-09 1953-04-28 Standard Oil Co Cracked naphtha desulfurization
US2717855A (en) * 1951-07-28 1955-09-13 Exxon Research Engineering Co Hydrodesulfurization of heavy oils
US2730487A (en) * 1952-07-14 1956-01-10 British Petroleum Co Removal of vanadium and/or sodium from petroleum and petroleum products with titania on alumina and hydrofining
US2766183A (en) * 1952-06-18 1956-10-09 British Petroleum Co Removal of vanadium and/or sodium from petroleum and petroleum products with fuller's earth
DE959488C (en) * 1952-04-01 1957-03-07 Ruhrchemie Ag Process to increase the knock resistance of gasoline from carbohydrate hydrogenation
DE1036436B (en) * 1955-10-18 1958-08-14 Still Fa Carl Process for heating hydrocarbons, in particular benzene hydrocarbons, for the purpose of catalytic refining
DE971558C (en) * 1951-03-20 1959-03-19 British Petroleum Co Process for the hydrocatalytic desulphurization of crude petroleum containing vanadium and sodium
US2944091A (en) * 1956-04-11 1960-07-05 Gelsenkirchener Bergwerks Ag Method of producing refined benzol
US3052742A (en) * 1959-06-15 1962-09-04 Sun Oil Co Removing nitrogen compounds from aromatic hydrocarbons by acid treatment
US3131231A (en) * 1956-10-27 1964-04-28 Cushman Darby And Cushman Process for purifying crude benzene
DE976855C (en) * 1951-10-18 1964-06-11 British Petroleum Co Process for hydrofining crude petroleum
DE1192358B (en) * 1955-04-02 1965-05-06 Carlo Padovani Process for the continuous production of heating oils from raw oils or raw oils
US3400169A (en) * 1964-01-20 1968-09-03 Exxon Research Engineering Co Preparation of steam cracked naphtha for benzene recovery
US4414102A (en) * 1981-05-15 1983-11-08 Mobil Oil Corporation Process for reducing nitrogen and/or oxygen heteroatom content of a mineral oil

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2542970A (en) * 1946-06-15 1951-02-27 Standard Oil Dev Co Refining of cracked naphthas by selective hydrogenation
US2636843A (en) * 1950-10-09 1953-04-28 Standard Oil Co Cracked naphtha desulfurization
DE971558C (en) * 1951-03-20 1959-03-19 British Petroleum Co Process for the hydrocatalytic desulphurization of crude petroleum containing vanadium and sodium
US2717855A (en) * 1951-07-28 1955-09-13 Exxon Research Engineering Co Hydrodesulfurization of heavy oils
DE976855C (en) * 1951-10-18 1964-06-11 British Petroleum Co Process for hydrofining crude petroleum
DE959488C (en) * 1952-04-01 1957-03-07 Ruhrchemie Ag Process to increase the knock resistance of gasoline from carbohydrate hydrogenation
US2766183A (en) * 1952-06-18 1956-10-09 British Petroleum Co Removal of vanadium and/or sodium from petroleum and petroleum products with fuller's earth
US2730487A (en) * 1952-07-14 1956-01-10 British Petroleum Co Removal of vanadium and/or sodium from petroleum and petroleum products with titania on alumina and hydrofining
DE1192358B (en) * 1955-04-02 1965-05-06 Carlo Padovani Process for the continuous production of heating oils from raw oils or raw oils
DE1036436B (en) * 1955-10-18 1958-08-14 Still Fa Carl Process for heating hydrocarbons, in particular benzene hydrocarbons, for the purpose of catalytic refining
US2944091A (en) * 1956-04-11 1960-07-05 Gelsenkirchener Bergwerks Ag Method of producing refined benzol
US3131231A (en) * 1956-10-27 1964-04-28 Cushman Darby And Cushman Process for purifying crude benzene
US3052742A (en) * 1959-06-15 1962-09-04 Sun Oil Co Removing nitrogen compounds from aromatic hydrocarbons by acid treatment
US3400169A (en) * 1964-01-20 1968-09-03 Exxon Research Engineering Co Preparation of steam cracked naphtha for benzene recovery
US4414102A (en) * 1981-05-15 1983-11-08 Mobil Oil Corporation Process for reducing nitrogen and/or oxygen heteroatom content of a mineral oil

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