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GB1232594A - - Google Patents

Info

Publication number
GB1232594A
GB1232594A GB3177067A GB1232594DA GB1232594A GB 1232594 A GB1232594 A GB 1232594A GB 3177067 A GB3177067 A GB 3177067A GB 1232594D A GB1232594D A GB 1232594DA GB 1232594 A GB1232594 A GB 1232594A
Authority
GB
United Kingdom
Prior art keywords
sulphur
stage
nickel
aromatics
hydrogen sulphide
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
GB3177067A
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 filed Critical
Publication of GB1232594A publication Critical patent/GB1232594A/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
    • C10G67/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only
    • C10G67/02—Treatment 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
    • C10G67/06—Treatment 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 a sorption process as the refining step in the absence of hydrogen
    • 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
    • C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
    • C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
    • C10G65/04—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps
    • C10G65/08—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps at least one step being a hydrogenation of the aromatic 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

1,232,594. Hydrotreating petroleum distillates. BRITISH PETROLEUM CO. Ltd. 2 July, 1968 [11 July, 1967], No. 31770/67. Heading C5E. A process for the desulphurization and dearomatization of a petroleum distillate boiling within the range 60‹ to 250‹ C. and containing up to 2% sulphur and up to 25 weight per cent aromatics comprises catalytically hydrodesulphurizing the distillate in a first stage to convert the major proportion of the sulphur to hydrogen sulphide, removing the hydrogen sulphide, contacting the fraction of reduced sulphur content with supported elemental nickel in a second stage under conditions such that residual sulphur is absorbed by the nickel without substantial liberation of hydrogen sulphide, without substantial hydrogenation of the aromatics, and without substantial hydrocracking of the feedstock, and hydrogenating the aromatics in a third stage over supported elemental nickel. The first stage catalyst may be cobalt oxide and molybdenum oxide on alumina; the preferred catalyst for the second and third stages is nickel on sepiolite.
GB3177067A 1967-07-11 1967-07-11 Expired GB1232594A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB3177067 1967-07-11

Publications (1)

Publication Number Publication Date
GB1232594A true GB1232594A (en) 1971-05-19

Family

ID=10328151

Family Applications (1)

Application Number Title Priority Date Filing Date
GB3177067A Expired GB1232594A (en) 1967-07-11 1967-07-11

Country Status (8)

Country Link
US (1) US3654139A (en)
AT (1) AT284313B (en)
BE (1) BE717938A (en)
DE (1) DE1770834A1 (en)
FR (1) FR1573585A (en)
GB (1) GB1232594A (en)
NL (1) NL6809779A (en)
NO (1) NO121735B (en)

Families Citing this family (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA958358A (en) * 1969-12-31 1974-11-26 Robert A. Johnson Petroleum fractions of low ultraviolet absorbance
US3732155A (en) * 1971-03-31 1973-05-08 Exxon Research Engineering Co Two-stage hydrodesulfurization process with hydrogen addition in the first stage
NL153934B (en) * 1973-02-02 1977-07-15 Basf Ag PROCEDURE FOR THE CATALYTIC HYDROGENATION OF AROMATICS, SULFUR AND NITROGEN COMPOUNDS CONTAINING MINERAL OIL FRACTIONS.
US4849093A (en) * 1987-02-02 1989-07-18 Union Oil Company Of California Catalytic aromatic saturation of hydrocarbons
JP3424053B2 (en) * 1994-09-02 2003-07-07 新日本石油株式会社 Method for producing low sulfur low aromatic gas oil
US6884531B2 (en) * 2001-05-21 2005-04-26 Saudi Arabian Oil Company Liquid hydrocarbon based fuels for fuel cell on-board reformers
JP4643966B2 (en) * 2004-10-01 2011-03-02 Ｊｘ日鉱日石エネルギー株式会社 Process for producing hydrorefined gas oil, hydrorefined gas oil and gas oil composition
US7842181B2 (en) * 2006-12-06 2010-11-30 Saudi Arabian Oil Company Composition and process for the removal of sulfur from middle distillate fuels
US8142646B2 (en) * 2007-11-30 2012-03-27 Saudi Arabian Oil Company Process to produce low sulfur catalytically cracked gasoline without saturation of olefinic compounds
US20090145808A1 (en) * 2007-11-30 2009-06-11 Saudi Arabian Oil Company Catalyst to attain low sulfur diesel
WO2009105749A2 (en) 2008-02-21 2009-08-27 Saudi Arabian Oil Company Catalyst to attain low sulfur gasoline
WO2011061576A1 (en) * 2009-11-20 2011-05-26 Total Raffinage Marketing Process for the production of hydrocarbon fluids having a low aromatic content
WO2011061575A1 (en) * 2009-11-20 2011-05-26 Total Raffinage Marketing Process for the production of hydrocarbon fluids having a low aromatic content
US9005432B2 (en) 2010-06-29 2015-04-14 Saudi Arabian Oil Company Removal of sulfur compounds from petroleum stream
US8535518B2 (en) 2011-01-19 2013-09-17 Saudi Arabian Oil Company Petroleum upgrading and desulfurizing process
FR3015514B1 (en) 2013-12-23 2016-10-28 Total Marketing Services IMPROVED PROCESS FOR DESAROMATIZATION OF PETROLEUM CUTTERS
US10752847B2 (en) 2017-03-08 2020-08-25 Saudi Arabian Oil Company Integrated hydrothermal process to upgrade heavy oil
US10703999B2 (en) 2017-03-14 2020-07-07 Saudi Arabian Oil Company Integrated supercritical water and steam cracking process
US10526552B1 (en) 2018-10-12 2020-01-07 Saudi Arabian Oil Company Upgrading of heavy oil for steam cracking process

Also Published As

Publication number Publication date
US3654139A (en) 1972-04-04
NL6809779A (en) 1969-01-14
NO121735B (en) 1971-04-05
BE717938A (en) 1969-01-13
AT284313B (en) 1970-09-10
FR1573585A (en) 1969-07-04
DE1770834A1 (en) 1972-01-13

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Legal Events

Date Code Title Description
PS Patent sealed [section 19, patents act 1949]
PCNP Patent ceased through non-payment of renewal fee