DK1612255T3 - Afsvovlingsfremgangsmåde til naphtafraktionen, der anvender en katalysator med styret porösitet - Google Patents

Afsvovlingsfremgangsmåde til naphtafraktionen, der anvender en katalysator med styret porösitet

Info

Publication number
DK1612255T3
DK1612255T3 DK05291383T DK05291383T DK1612255T3 DK 1612255 T3 DK1612255 T3 DK 1612255T3 DK 05291383 T DK05291383 T DK 05291383T DK 05291383 T DK05291383 T DK 05291383T DK 1612255 T3 DK1612255 T3 DK 1612255T3
Authority
DK
Denmark
Prior art keywords
naphtha fraction
controlled porosity
sulfurization process
porosity catalyst
catalyst
Prior art date
Application number
DK05291383T
Other languages
English (en)
Other versions
DK1612255T4 (da
Inventor
Christophe Bouchy
Nathalie Marchal
Florent Picard
Original Assignee
Inst Francais Du Petrole
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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=34946714&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=DK1612255(T3) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Inst Francais Du Petrole filed Critical Inst Francais Du Petrole
Application granted granted Critical
Publication of DK1612255T3 publication Critical patent/DK1612255T3/da
Publication of DK1612255T4 publication Critical patent/DK1612255T4/da

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
    • C10G45/04Refining 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 characterised by the catalyst used
    • C10G45/06Refining 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 characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof
    • 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
    • C10G45/04Refining 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 characterised by the catalyst used
    • 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
    • C10G45/04Refining 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 characterised by the catalyst used
    • C10G45/06Refining 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 characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof
    • C10G45/08Refining 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 characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof in combination with chromium, molybdenum, or tungsten metals, or compounds thereof
    • 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
    • C10G2300/00Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10Feedstock materials
    • C10G2300/1037Hydrocarbon fractions
    • C10G2300/1044Heavy gasoline or naphtha having a boiling range of about 100 - 180 °C
    • 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
    • C10G2300/00Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/20Characteristics of the feedstock or the products
    • C10G2300/201Impurities
    • C10G2300/202Heteroatoms content, i.e. S, N, O, P
    • 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
    • C10G2400/00Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/02Gasoline

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)
DK05291383.7T 2004-07-01 2005-06-27 Afsvovlingsfremgangsmåde til naphthafraktionen, der anvender en katalysator med styret porøsitet DK1612255T4 (da)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR0407335A FR2872516B1 (fr) 2004-07-01 2004-07-01 Procede d'hydrodesulfuration des essences mettant en oeuvre un catalyseur a porosite controlee

Publications (2)

Publication Number Publication Date
DK1612255T3 true DK1612255T3 (da) 2008-03-17
DK1612255T4 DK1612255T4 (da) 2016-07-11

Family

ID=34946714

Family Applications (1)

Application Number Title Priority Date Filing Date
DK05291383.7T DK1612255T4 (da) 2004-07-01 2005-06-27 Afsvovlingsfremgangsmåde til naphthafraktionen, der anvender en katalysator med styret porøsitet

Country Status (8)

Country Link
US (2) US20060000751A1 (da)
EP (1) EP1612255B2 (da)
KR (1) KR101209347B1 (da)
BR (1) BRPI0502597B1 (da)
CA (1) CA2510668C (da)
DE (1) DE602005003402T3 (da)
DK (1) DK1612255T4 (da)
FR (1) FR2872516B1 (da)

Families Citing this family (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101399700B1 (ko) 2006-01-17 2014-05-26 엑손모빌 리서치 앤드 엔지니어링 컴퍼니 나프타 수소첨가탈황을 위한 고온 알루미나 지지체를 가진 선택적 촉매
EP1976631A2 (en) * 2006-01-17 2008-10-08 ExxonMobil Research and Engineering Company Selective catalysts for naphtha hydrodesulfurization
US8216958B2 (en) * 2006-01-17 2012-07-10 Exxonmobil Research And Engineering Company Selective catalysts having silica supports for naphtha hydrodesulfurization
EP2915868B1 (en) * 2006-01-17 2016-12-21 ExxonMobil Research and Engineering Company Selective catalysts for naphtha hydrodesulfurization
FR2908781B1 (fr) * 2006-11-16 2012-10-19 Inst Francais Du Petrole Procede de desulfuration profonde des essences de craquage avec une faible perte en indice d'octane
US7749375B2 (en) * 2007-09-07 2010-07-06 Uop Llc Hydrodesulfurization process
US20090223867A1 (en) * 2008-03-06 2009-09-10 Opinder Kishan Bhan Catalyst and process for the selective hydrodesulfurization of an olefin containing hydrocarbon feedstock
US20090223864A1 (en) * 2008-03-06 2009-09-10 Opinder Kishan Bhan Process for the selective hydrodesulfurization of an olefin containing hydrocarbon feedstock
US20090223866A1 (en) * 2008-03-06 2009-09-10 Opinder Kishan Bhan Process for the selective hydrodesulfurization of a gasoline feedstock containing high levels of olefins
US20090223868A1 (en) * 2008-03-06 2009-09-10 Opinder Kishan Bhan Catalyst and process for the selective hydrodesulfurization of an olefin containing hydrocarbon feedstock
JP5405585B2 (ja) * 2008-11-26 2014-02-05 エスケー イノベーション カンパニー リミテッド 流動層接触分解留分からクリーン燃料および芳香族製品を製造する方法
JP6117203B2 (ja) 2011-07-29 2017-04-19 サウジ アラビアン オイル カンパニー 中間留分の選択的水素化処理方法
FR2994864B1 (fr) 2012-09-05 2015-08-21 IFP Energies Nouvelles Procede de sulfuration d'un catalyseur d'hydrodesulfuration
EP2816094B1 (fr) 2013-06-19 2020-04-29 IFP Energies nouvelles Procédé de production d'une essence à basse teneur en soufre et en mercaptans
US9822317B2 (en) 2014-10-10 2017-11-21 Uop Llc Process and apparatus for selectively hydrogenating naphtha
US9393538B2 (en) 2014-10-10 2016-07-19 Uop Llc Process and apparatus for selectively hydrogenating naphtha
FR3094985B1 (fr) 2019-04-12 2021-04-02 Axens Procédé d’hydrotraitement d’un naphta
FR3116825A1 (fr) 2020-11-27 2022-06-03 IFP Energies Nouvelles Procédé d’hydrodésulfuration d’une coupe essence mettant en œuvre un catalyseur ayant une porosité bimodale particulière

Family Cites Families (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU513580B2 (en) 1976-03-04 1980-12-11 Amoco Corporation The selective desulfurization of cracked naphthas
US4203829A (en) 1978-09-28 1980-05-20 Standard Oil Company (Indiana) Catalyst, method of preparation and use thereof in hydrodesulfurizing cracked naphtha
CA1195278A (en) * 1981-09-28 1985-10-15 Chevron Research And Technology Company Layered residua treatment catalyst process and temperature profile
US5287708A (en) 1990-09-28 1994-02-22 Kabushiki Kaisha Toyoda Jidoshokki Seisakusho Car air conditioner with a hydraulically driven refrigerant compressor
US5318690A (en) 1991-08-15 1994-06-07 Mobil Oil Corporation Gasoline upgrading process
US5423975A (en) * 1992-07-08 1995-06-13 Texaco Inc. Selective hydrodesulfurization of naphtha using spent resid catalyst
JPH08507468A (ja) * 1993-03-12 1996-08-13 トリコム・インコーポレーテッド 触媒再生
US5340466A (en) 1993-04-19 1994-08-23 Texaco Inc. Hydrodesulfurization of cracked naphtha with hydrotalcite-containing catalyst
US5525211A (en) 1994-10-06 1996-06-11 Texaco Inc. Selective hydrodesulfurization of naphtha using selectively poisoned hydroprocessing catalyst
US5770046A (en) 1995-03-17 1998-06-23 Texaco Inc Selective hydrodesulfurization of cracked naphtha using novel catalysts
US6409913B1 (en) 1996-02-02 2002-06-25 Exxonmobil Research And Engineering Company Naphtha desulfurization with reduced mercaptan formation
US6013598A (en) 1996-02-02 2000-01-11 Exxon Research And Engineering Co. Selective hydrodesulfurization catalyst
US6231754B1 (en) 1996-02-02 2001-05-15 Exxon Research And Engineering Company High temperature naphtha desulfurization using a low metal and partially deactivated catalyst
US6231753B1 (en) 1996-02-02 2001-05-15 Exxon Research And Engineering Company Two stage deep naphtha desulfurization with reduced mercaptan formation
FR2764298B1 (fr) * 1997-06-10 1999-07-16 Inst Francais Du Petrole Hydrotraitement de charges hydrocarbonees dans un reacteur en lit bouillonnant
US6435273B1 (en) 1998-12-14 2002-08-20 Vladlen Futernik Device for air temperature control in a vehicle
FR2790000B1 (fr) 1999-02-24 2001-04-13 Inst Francais Du Petrole Procede de production d'essences a faible teneur en soufre
FR2797639B1 (fr) 1999-08-19 2001-09-21 Inst Francais Du Petrole Procede de production d'essences a faible teneur en soufre
US6793016B2 (en) 2000-01-28 2004-09-21 Denso Corporation Vehicle air conditioning system with seat air conditioning unit
US20020148758A1 (en) * 2001-02-08 2002-10-17 Yun-Feng Chang Gasoline hydrodesulfurization
JP3659213B2 (ja) 2001-10-30 2005-06-15 日産自動車株式会社 車両用冷却装置
US7297251B2 (en) 2002-05-21 2007-11-20 Exxonmobil Research And Engineering Company Multi-stage hydrodesulfurization of cracked naphtha streams with a stacked bed reactor
US7069938B2 (en) 2003-11-18 2006-07-04 Yo Fu Umbrella Co., Ltd. Golf sunshade
BRPI0601787B1 (pt) * 2006-05-17 2016-06-07 Petroleo Brasileiro Sa processo de hidrodessulfurização seletiva de nafta

Also Published As

Publication number Publication date
FR2872516B1 (fr) 2007-03-09
US20120067780A1 (en) 2012-03-22
CA2510668A1 (fr) 2006-01-01
US20060000751A1 (en) 2006-01-05
EP1612255A1 (fr) 2006-01-04
EP1612255B2 (fr) 2016-03-30
DE602005003402T2 (de) 2008-02-28
CA2510668C (fr) 2013-01-29
KR20060049757A (ko) 2006-05-19
DE602005003402D1 (de) 2008-01-03
DK1612255T4 (da) 2016-07-11
FR2872516A1 (fr) 2006-01-06
DE602005003402T3 (de) 2016-07-21
BRPI0502597A (pt) 2006-02-14
US8926831B2 (en) 2015-01-06
EP1612255B1 (fr) 2007-11-21
KR101209347B1 (ko) 2012-12-06
BRPI0502597B1 (pt) 2014-12-30

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