GB732387A - Improved method for manufacturing heating oil - Google Patents

Improved method for manufacturing heating oil

Info

Publication number
GB732387A
GB732387A GB29690/52A GB2969052A GB732387A GB 732387 A GB732387 A GB 732387A GB 29690/52 A GB29690/52 A GB 29690/52A GB 2969052 A GB2969052 A GB 2969052A GB 732387 A GB732387 A GB 732387A
Authority
GB
United Kingdom
Prior art keywords
heating oil
virgin
treatment
fraction
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
GB29690/52A
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.)
Standard Oil Development Co
Original Assignee
Standard Oil Development Co
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 Standard Oil Development Co filed Critical Standard Oil Development Co
Publication of GB732387A publication Critical patent/GB732387A/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
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/04—Liquid carbonaceous fuels essentially based on blends of hydrocarbons
    • 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
    • C10G2400/06—Gasoil

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)
  • Catalysts (AREA)

Abstract

A mineral heating oil composition, boiling within the range 300-750 DEG F., having little tendency to deposit carbon when burnt and also useful as a diesel fuel, is prepared by contacting a virgin heating oil with hydrogen in the presence of a hydrogenation catalyst, under temperature and pressure conditions such that the consumption of hydrogen is not more than 60 cubic feet per barrel, and blending the product with a heating oil obtained in a cracking operation. A process is described in which crude petroleum is fractionated by distillation to yield a virgin heating oil fraction, a gas oil fraction and other fractions. The virgin heating oil fraction is partially desulphurized by hydrofining with the above-mentioned hydrogen consumption, for example at 400-700 DEG F. and 50-250 lbs./sq. in. pressure using a cobalt molybdate or molybdenum oxide catalyst supported on a carrier such as alumina. The hydrofined fraction may be steam stripped or washed with caustic alkali to remove traces of hydrogen sulphide before blending with the cracked heating oil mentioned below. The gas oil fraction is passed to a cracking zone wherein it is subjected to thermal or catalytic cracking, particularly catalytic cracking in presence of a fluidized catalyst, and the cracking products are fractionated to yield a heating oil fraction and other fractions. This heating oil fraction may be washed with caustic alkali before blending with the hydrofined virgin heating oil mentioned above. The blend prepared according to the invention is compared with other blends of sweetened virgin heating oil and cracked heating oil wherein the virgin heating oil is sweetened by (i) doctor treatment, (ii) treatment with lead sulphide and sulphur, (iii) treatment with air and caustic soda, (iv) hypochlorite treatment, or (v) treatment with methyl alcohol and caustic soda.
GB29690/52A 1952-02-14 1952-11-24 Improved method for manufacturing heating oil Expired GB732387A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US271556A US2717857A (en) 1952-02-14 1952-02-14 Method for manufacturing heating oil

Publications (1)

Publication Number Publication Date
GB732387A true GB732387A (en) 1955-06-22

Family

ID=23036089

Family Applications (1)

Application Number Title Priority Date Filing Date
GB29690/52A Expired GB732387A (en) 1952-02-14 1952-11-24 Improved method for manufacturing heating oil

Country Status (3)

Country Link
US (1) US2717857A (en)
BE (1) BE545907A (en)
GB (1) GB732387A (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2891006A (en) * 1954-08-26 1959-06-16 Hydrocarbon Research Inc Method of stabilizing olefinic gasoline by hydrofining with a chromium iron oxide catalyst
US2840512A (en) * 1955-09-29 1958-06-24 Kellogg M W Co Stabilization of furnace oil by hydrotreating to remove sulfur and gum
US2936281A (en) * 1956-06-26 1960-05-10 Pure Oil Co Refining process
US2951033A (en) * 1958-03-28 1960-08-30 Atlantic Refining Co Process for preparing stable heating oil
US3424673A (en) * 1966-03-07 1969-01-28 Sun Oil Co Process for hydrodesulfurizing the lower boiling fraction of a cracked gas oil blend
US3870626A (en) * 1973-02-27 1975-03-11 Gulf Research Development Co Method for reducing the mercaptan content of a middle distillate oil
US3876532A (en) * 1973-02-27 1975-04-08 Gulf Research Development Co Method for reducing the total acid number of a middle distillate oil
US3850744A (en) * 1973-02-27 1974-11-26 Gulf Research Development Co Method for utilizing a fixed catalyst bed in separate hydrogenation processes

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2347515A (en) * 1940-04-11 1944-04-25 Standard Oil Dev Co Refining mineral oils
US2547380A (en) * 1945-10-01 1951-04-03 Union Oil Co Catalyst for hydrocarbon conversion
US2577823A (en) * 1948-02-06 1951-12-11 Standard Oil Co Hydrodesulfurization of sulfurcontaining hydrocarbon fractions
US2574447A (en) * 1948-06-01 1951-11-06 Anglo Iranian Oil Co Ltd Catalytic desulfurization of petroleum hydrocarbons
US2574448A (en) * 1948-06-24 1951-11-06 Anglo Iranian Oil Co Ltd Catalytic desulfurization of gas oil
FR989481A (en) * 1948-06-24 1951-09-10 Anglo Iranian Oil Co Ltd Catalytic desulfurization process of petroleum distillates
US2592383A (en) * 1949-06-28 1952-04-08 Standard Oil Dev Co Process for preparing heating oil

Also Published As

Publication number Publication date
US2717857A (en) 1955-09-13
BE545907A (en)

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