GB1205481A - Desulfurization process - Google Patents

Desulfurization process

Info

Publication number
GB1205481A
GB1205481A GB00981/68A GB1098168A GB1205481A GB 1205481 A GB1205481 A GB 1205481A GB 00981/68 A GB00981/68 A GB 00981/68A GB 1098168 A GB1098168 A GB 1098168A GB 1205481 A GB1205481 A GB 1205481A
Authority
GB
United Kingdom
Prior art keywords
boiling
asphaltic fraction
sulphur
desulphurized
asphaltic
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
GB00981/68A
Inventor
Norman Johnstone Paterson
Ronald Reginald Roselius
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.)
Chevron USA Inc
Original Assignee
Chevron Research and Technology Co
Chevron Research 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 Chevron Research and Technology Co, Chevron Research Co filed Critical Chevron Research and Technology Co
Publication of GB1205481A publication Critical patent/GB1205481A/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
    • 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
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/02—Refining 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
    • 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

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

1,205,481. Desulphurizing oil. CHEVRON RESEARCH CO. 6 March, 1968 [10 March, 1967], No. 10981/68. Heading C5E. A process for the production of low sulphur content heavy fuel oil containing not more than 2 weight per cent sulphur from high sulphur content petroleum residua containing more than 2 weight per cent of sulphur comprises separating high sulphur petroleum residue boiling at 650‹ F. or above into an asphaltic fraction and a non-asphaltic fraction, subjecting the non- asphaltic fraction to a catalytic hydrodesulphurization treatment, wherein the desulphurization of the non-asphaltic fraction is carried out in admixture with light distillate boiling at a temperature of from 300‹ F. to 700‹ F. and at least partly in the kerosene boiling range, said distillate being present in amount effective substantially to inhibit hydrocracking of said non- asphaltic fraction during the hydrodesulphurization, separating light distillate boiling at up to 700‹ F. from desulphurized non-asphaltic fraction boiling at 650‹ F. or above in the desulphurized mixture, and thereafter blending the resulting desulphurized non-asphaltic fraction with the asphaltic fraction to produce the required low sulphur content heavy fuel oil. A preferred catalyst comprises alumina and silica promoted with molybdenum and nickel. If the light distillate which may be kerosene or light diesel fuel also contains sulphur it is also desulphurized in the process. The examples disclose treatment of (1) all that part of a crude oil boiling above the middle distillate range, and (2) a vacuum gas oil.
GB00981/68A 1967-03-10 1968-03-06 Desulfurization process Expired GB1205481A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US62228967A 1967-03-10 1967-03-10

Publications (1)

Publication Number Publication Date
GB1205481A true GB1205481A (en) 1970-09-16

Family

ID=24493642

Family Applications (1)

Application Number Title Priority Date Filing Date
GB00981/68A Expired GB1205481A (en) 1967-03-10 1968-03-06 Desulfurization process

Country Status (7)

Country Link
US (1) US3464915A (en)
JP (1) JPS4933561B1 (en)
DE (1) DE1645720A1 (en)
ES (1) ES351438A1 (en)
FR (1) FR1559217A (en)
GB (1) GB1205481A (en)
NL (1) NL6803379A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1130080A1 (en) * 1998-10-30 2001-09-05 JGC Corporation Gas turbine fuel oil and production method thereof and power generation method
WO2009126974A2 (en) * 2008-04-10 2009-10-15 Shell Oil Company Diluents, method for preparing a diluted hydrocarbon composition, and diluted hydrocarbon compositions
US8450538B2 (en) 2008-04-10 2013-05-28 Shell Oil Company Hydrocarbon composition

Families Citing this family (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3666659A (en) * 1970-03-24 1972-05-30 Gulf Research Development Co Method for stabilizing hydrodesulfurized oil
US3708569A (en) * 1970-12-17 1973-01-02 Cities Service Res & Dev Co Burning unconverted h-oil residual
US3997430A (en) * 1973-03-29 1976-12-14 Gulf Research & Development Company Hydrodesulfurization process involving blending high boiling streams
US3912621A (en) * 1973-12-07 1975-10-14 Texaco Inc Hydro desulfurization of heavy petroleum oil at higher temperatures and space velocities
US4629553A (en) * 1985-07-31 1986-12-16 Exxon Research And Engineering Company Hydrofining process
JPS63258985A (en) * 1987-04-16 1988-10-26 Kawasaki Heavy Ind Ltd Hydrogenation treatment of heavy oil
US4885080A (en) * 1988-05-25 1989-12-05 Phillips Petroleum Company Process for demetallizing and desulfurizing heavy crude oil
DK29598A (en) * 1998-03-04 1999-09-05 Haldor Topsoe As Process for desulphurizing FCC heavy gasoline
JP5421794B2 (en) * 2010-01-12 2014-02-19 日揮株式会社 Crude oil processing system
JP5421793B2 (en) * 2010-01-12 2014-02-19 日揮株式会社 Crude oil processing system
US9109176B2 (en) 2011-03-28 2015-08-18 Exxonmobil Research And Engineering Company Method for making marine bunker fuels
FI20175815A1 (en) 2017-09-14 2019-03-15 Neste Oyj Low sulfur fuel oil bunker composition and process for producing the same
US10899983B1 (en) 2020-05-22 2021-01-26 Exxonmobil Research And Engineering Company High napthenic content marine fuel compositions

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2988501A (en) * 1958-08-18 1961-06-13 Union Oil Co Hydrorefining of crude oils
NL276254A (en) * 1961-03-25

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1130080A1 (en) * 1998-10-30 2001-09-05 JGC Corporation Gas turbine fuel oil and production method thereof and power generation method
EP1130080A4 (en) * 1998-10-30 2004-11-24 Jgc Corp Gas turbine fuel oil and production method thereof and power generation method
US7276151B1 (en) 1998-10-30 2007-10-02 Jgc Corporation Gas turbine fuel oil and production method thereof and power generation method
WO2009126974A2 (en) * 2008-04-10 2009-10-15 Shell Oil Company Diluents, method for preparing a diluted hydrocarbon composition, and diluted hydrocarbon compositions
WO2009126974A3 (en) * 2008-04-10 2010-03-18 Shell Oil Company Method for preparing a diluted hydrocarbon composition, and diluted hydrocarbon compositions
US8450538B2 (en) 2008-04-10 2013-05-28 Shell Oil Company Hydrocarbon composition
US8734634B2 (en) 2008-04-10 2014-05-27 Shell Oil Company Method for producing a crude product, method for preparing a diluted hydrocarbon composition, crude products, diluents and uses of such crude products and diluents

Also Published As

Publication number Publication date
US3464915A (en) 1969-09-02
NL6803379A (en) 1968-09-11
DE1645720A1 (en) 1970-08-06
FR1559217A (en) 1969-03-07
ES351438A1 (en) 1969-12-01
JPS4933561B1 (en) 1974-09-07

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Legal Events

Date Code Title Description
PS Patent sealed [section 19, patents act 1949]
PLNP Patent lapsed through nonpayment of renewal fees