EP1818385A4 - Process for producing hydrorefined gas oil, hydrorefind gas oil, and gas oil composition - Google Patents

Process for producing hydrorefined gas oil, hydrorefind gas oil, and gas oil composition

Info

Publication number
EP1818385A4
EP1818385A4 EP05788266A EP05788266A EP1818385A4 EP 1818385 A4 EP1818385 A4 EP 1818385A4 EP 05788266 A EP05788266 A EP 05788266A EP 05788266 A EP05788266 A EP 05788266A EP 1818385 A4 EP1818385 A4 EP 1818385A4
Authority
EP
European Patent Office
Prior art keywords
gas oil
total
volume
content
oil
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.)
Withdrawn
Application number
EP05788266A
Other languages
German (de)
French (fr)
Japanese (ja)
Other versions
EP1818385A1 (en
Inventor
Hideshi Iki
Yukihiro Sugiura
Yuichi Tanaka
Hirofumi Konno
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.)
Eneos Corp
Original Assignee
Nippon Oil Corp
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 Nippon Oil Corp filed Critical Nippon Oil Corp
Publication of EP1818385A1 publication Critical patent/EP1818385A1/en
Publication of EP1818385A4 publication Critical patent/EP1818385A4/en
Withdrawn legal-status Critical Current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
    • C10G45/44—Hydrogenation of the aromatic hydrocarbons
    • C10G45/46—Hydrogenation of the aromatic hydrocarbons characterised by the catalyst used
    • C10G45/52—Hydrogenation of the aromatic hydrocarbons characterised by the catalyst used containing platinum group metals or compounds thereof
    • 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
    • C10G65/12—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including cracking steps and other hydrotreatment steps
    • 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
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/20—Characteristics of the feedstock or the products
    • C10G2300/201—Impurities
    • C10G2300/202—Heteroatoms content, i.e. S, N, O, P
    • 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
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/20—Characteristics of the feedstock or the products
    • C10G2300/30—Physical properties of feedstocks or products
    • C10G2300/301—Boiling range
    • 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)

Abstract

This invention provides a process for producing a hydrorefined gas oil, comprising the step of hydrogenating a hydrorefining oil containing not less than 95% by volume of a distillation fraction having a boiling point range of 150 to 380ºC and having a sulfur content of 2 to 15 ppm by mass, a total aromatic content of 10 to 25% by volume, and a total naphthene content of 20 to 60% by volume in the presence of a hydrogenation catalyst to prepare a generated oil having a total aromatic content of not more than 3% by volume, and the step of hydrogenating the above generated oil in the presence of a hydrogenation catalyst comprising a crystalline molecular sieve component to prepare a generated oil containing not more than 16% by volume of a petroleum distillation fraction having a boiling point range of below 150ºC and satisfying the requirement that the total of the total aromatic content and the total naphthene content is not more than 80% of the total of the total aromatic content and the total naphthene content in the hydrorefining oil.
EP05788266A 2004-10-01 2005-09-30 Process for producing hydrorefined gas oil, hydrorefind gas oil, and gas oil composition Withdrawn EP1818385A4 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2004290672A JP4643966B2 (en) 2004-10-01 2004-10-01 Process for producing hydrorefined gas oil, hydrorefined gas oil and gas oil composition
PCT/JP2005/018127 WO2006038555A1 (en) 2004-10-01 2005-09-30 Process for producing hydrorefined gas oil, hydrorefind gas oil, and gas oil composition

Publications (2)

Publication Number Publication Date
EP1818385A1 EP1818385A1 (en) 2007-08-15
EP1818385A4 true EP1818385A4 (en) 2008-12-17

Family

ID=36142629

Family Applications (1)

Application Number Title Priority Date Filing Date
EP05788266A Withdrawn EP1818385A4 (en) 2004-10-01 2005-09-30 Process for producing hydrorefined gas oil, hydrorefind gas oil, and gas oil composition

Country Status (4)

Country Link
US (1) US20080308459A1 (en)
EP (1) EP1818385A4 (en)
JP (1) JP4643966B2 (en)
WO (1) WO2006038555A1 (en)

Families Citing this family (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4854075B2 (en) * 2006-06-28 2012-01-11 Ｊｘ日鉱日石エネルギー株式会社 Method for producing ultra-low sulfur gas oil base and ultra-low sulfur gas oil composition comprising the ultra-low sulfur gas oil base
JP2010215723A (en) * 2009-03-13 2010-09-30 Idemitsu Kosan Co Ltd Method of manufacturing base material of gas oil
JP5379062B2 (en) * 2010-03-31 2013-12-25 Ｊｘ日鉱日石エネルギー株式会社 Process for producing light oil base or light oil composition
DE102011118482A1 (en) * 2011-11-12 2013-05-16 Volkswagen Aktiengesellschaft Increasing cetane number of naphtha comprises hydrogenation of used naphtha containing unsaturated and/or aryl compounds in presence of catalyst containing iridium or rhodium and/or oxidic carrier, and/or ring opening of cyclic compound
SG11201701405YA (en) * 2014-10-28 2017-05-30 Exxonmobil Res & Eng Co Catalyst configuration for increase hydrocracking activity
US9938475B2 (en) 2014-10-28 2018-04-10 Exxonmobil Research And Engineering Company Catalyst configuration for increased hydrocracking activity
US10550335B2 (en) 2015-12-28 2020-02-04 Exxonmobil Research And Engineering Company Fluxed deasphalter rock fuel oil blend component oils
US10590360B2 (en) 2015-12-28 2020-03-17 Exxonmobil Research And Engineering Company Bright stock production from deasphalted oil
US10947464B2 (en) 2015-12-28 2021-03-16 Exxonmobil Research And Engineering Company Integrated resid deasphalting and gasification
US10494579B2 (en) 2016-04-26 2019-12-03 Exxonmobil Research And Engineering Company Naphthene-containing distillate stream compositions and uses thereof
US12071592B2 (en) 2017-02-12 2024-08-27 Magēmā Technology LLC Multi-stage process and device utilizing structured catalyst beds and reactive distillation for the production of a low sulfur heavy marine fuel oil
US11788017B2 (en) 2017-02-12 2023-10-17 Magëmã Technology LLC Multi-stage process and device for reducing environmental contaminants in heavy marine fuel oil
US20180230389A1 (en) 2017-02-12 2018-08-16 Magēmā Technology, LLC Multi-Stage Process and Device for Reducing Environmental Contaminates in Heavy Marine Fuel Oil
US10604709B2 (en) 2017-02-12 2020-03-31 Magēmā Technology LLC Multi-stage device and process for production of a low sulfur heavy marine fuel oil from distressed heavy fuel oil materials
US12025435B2 (en) 2017-02-12 2024-07-02 Magēmã Technology LLC Multi-stage device and process for production of a low sulfur heavy marine fuel oil

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB824635A (en) * 1958-07-08 1959-12-02 Exxon Research Engineering Co Process for improving kerosenes and diesel fuels
GB834776A (en) * 1957-11-26 1960-05-11 Bataafsche Petroleum A method of preparing a liquid hydrocarbon fuel having a high heat of combustion perunit volume
US3654139A (en) * 1967-07-11 1972-04-04 John Winsor Desulphurisation and de-aromatisation of petroleum distillates
US3767562A (en) * 1971-09-02 1973-10-23 Lummus Co Production of jet fuel
US4469590A (en) * 1983-06-17 1984-09-04 Exxon Research And Engineering Co. Process for the hydrogenation of aromatic hydrocarbons
WO2002007881A1 (en) * 2000-07-21 2002-01-31 Exxonmobil Research And Engineering Company Naphthene ring opening over an iridium ring opening catalyst
US20020121457A1 (en) * 1998-12-30 2002-09-05 Tsao Ying-Yen P. Selective ring opening process for producing diesel fuel with increased cetane number

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3512317B2 (en) * 1996-12-24 2004-03-29 財団法人石油産業活性化センター Catalyst for hydrotreating hydrocarbon oil and method for hydrotreating light oil
JP3537979B2 (en) * 1996-12-24 2004-06-14 財団法人石油産業活性化センター Catalyst for hydrotreating hydrocarbon oil and method for hydrotreating light oil
US6210563B1 (en) * 1998-12-30 2001-04-03 Mobil Oil Corporation Process for producing diesel fuel with increased cetane number
US6623626B2 (en) * 2000-07-21 2003-09-23 Exxonmobil Research And Engineering Company Naphthene ring opening over a ring opening catalyst combination
US6683020B2 (en) * 2000-07-21 2004-01-27 Exxonmobil Research And Engineering Company Naphthene ring opening over an iridium ring opening catalyst

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB834776A (en) * 1957-11-26 1960-05-11 Bataafsche Petroleum A method of preparing a liquid hydrocarbon fuel having a high heat of combustion perunit volume
GB824635A (en) * 1958-07-08 1959-12-02 Exxon Research Engineering Co Process for improving kerosenes and diesel fuels
US3654139A (en) * 1967-07-11 1972-04-04 John Winsor Desulphurisation and de-aromatisation of petroleum distillates
US3767562A (en) * 1971-09-02 1973-10-23 Lummus Co Production of jet fuel
US4469590A (en) * 1983-06-17 1984-09-04 Exxon Research And Engineering Co. Process for the hydrogenation of aromatic hydrocarbons
US20020121457A1 (en) * 1998-12-30 2002-09-05 Tsao Ying-Yen P. Selective ring opening process for producing diesel fuel with increased cetane number
WO2002007881A1 (en) * 2000-07-21 2002-01-31 Exxonmobil Research And Engineering Company Naphthene ring opening over an iridium ring opening catalyst

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of WO2006038555A1 *

Also Published As

Publication number Publication date
EP1818385A1 (en) 2007-08-15
JP2006104271A (en) 2006-04-20
JP4643966B2 (en) 2011-03-02
US20080308459A1 (en) 2008-12-18
WO2006038555A1 (en) 2006-04-13

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