DE602005003402D1 - Hydroentschwefelungsverfahren für Benzine unter Verwendung eines Katalysators mit geregelter Porosität. - Google Patents

Hydroentschwefelungsverfahren für Benzine unter Verwendung eines Katalysators mit geregelter Porosität.

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Publication number
DE602005003402D1
DE602005003402D1 DE602005003402T DE602005003402T DE602005003402D1 DE 602005003402 D1 DE602005003402 D1 DE 602005003402D1 DE 602005003402 T DE602005003402 T DE 602005003402T DE 602005003402 T DE602005003402 T DE 602005003402T DE 602005003402 D1 DE602005003402 D1 DE 602005003402D1
Authority
DE
Germany
Prior art keywords
gasolines
controlled porosity
hydrodesulfurization process
porosity catalyst
catalyst
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.)
Active
Application number
DE602005003402T
Other languages
English (en)
Other versions
DE602005003402T3 (de
DE602005003402T2 (de
Inventor
Christophe Bouchy
Nathalie Marchal
Florent Picard
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.)
IFP Energies Nouvelles IFPEN
Original Assignee
IFP Energies Nouvelles IFPEN
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
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Application filed by IFP Energies Nouvelles IFPEN filed Critical IFP Energies Nouvelles IFPEN
Publication of DE602005003402D1 publication Critical patent/DE602005003402D1/de
Application granted granted Critical
Publication of DE602005003402T2 publication Critical patent/DE602005003402T2/de
Publication of DE602005003402T3 publication Critical patent/DE602005003402T3/de
Active legal-status Critical Current
Anticipated expiration legal-status Critical

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
    • C10G45/04—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 characterised by the catalyst used
    • 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
    • C10G45/04—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 characterised by the catalyst used
    • C10G45/06—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 characterised by the catalyst used containing nickel or cobalt metal, 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
    • 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
    • C10G45/04—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 characterised by the catalyst used
    • C10G45/06—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 characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof
    • C10G45/08—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 characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof in combination with chromium, molybdenum, or tungsten 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
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10—Feedstock materials
    • C10G2300/1037—Hydrocarbon fractions
    • C10G2300/1044—Heavy gasoline or naphtha having a boiling range of about 100 - 180 °C
    • 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
    • C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/02—Gasoline
DE602005003402.1T 2004-07-01 2005-06-27 Hydroentschwefelungsverfahren für Benzine unter Verwendung eines Katalysators mit geregelter Porosität. Active DE602005003402T3 (de)

Applications Claiming Priority (3)

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
FR0407335 2004-07-01
EP05291383.7A EP1612255B2 (de) 2004-07-01 2005-06-27 Hydroentschwefelungsverfahren für Benzine unter Verwendung eines Katalysators mit geregelter Porosität.

Publications (3)

Publication Number Publication Date
DE602005003402D1 true DE602005003402D1 (de) 2008-01-03
DE602005003402T2 DE602005003402T2 (de) 2008-02-28
DE602005003402T3 DE602005003402T3 (de) 2016-07-21

Family

ID=34946714

Family Applications (1)

Application Number Title Priority Date Filing Date
DE602005003402.1T Active DE602005003402T3 (de) 2004-07-01 2005-06-27 Hydroentschwefelungsverfahren für Benzine unter Verwendung eines Katalysators mit geregelter Porosität.

Country Status (8)

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

Families Citing this family (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2619363T3 (es) * 2006-01-17 2017-06-26 Exxonmobil Research And Engineering Company Catalizadores selectivos para la hidrodesulfuración de nafta
US8637423B2 (en) * 2006-01-17 2014-01-28 Exxonmobil Research And Engineering Company Selective catalysts having high temperature alumina supports for naphtha hydrodesulfurization
WO2007084438A2 (en) * 2006-01-17 2007-07-26 Exxonmobil Research And Engineering Company Selective catalysts for naphtha hydrodesulfurization
CA2636177C (en) 2006-01-17 2015-10-06 Exxonmobil Research And Engineering Company Selective catalysts having silica supports 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
US20090223868A1 (en) * 2008-03-06 2009-09-10 Opinder Kishan Bhan Catalyst and 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
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
WO2010061986A1 (en) * 2008-11-26 2010-06-03 Sk Energy Co., Ltd. Process for the preparation of clean fuel and aromatics from hydrocarbon mixtures catalytic cracked on fluid bed
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 (de) 2013-06-19 2020-04-29 IFP Energies nouvelles Herstellungsverfahren einer essenz mit niedrigem schwefel- und mercaptangehalt
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

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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
WO1994020213A1 (en) * 1993-03-12 1994-09-15 Tricom, Inc. Catalyst regeneration
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
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
US6409913B1 (en) 1996-02-02 2002-06-25 Exxonmobil Research And Engineering Company Naphtha desulfurization with reduced mercaptan formation
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
CA2510668A1 (fr) 2006-01-01
EP1612255A1 (de) 2006-01-04
DE602005003402T3 (de) 2016-07-21
DK1612255T3 (da) 2008-03-17
CA2510668C (fr) 2013-01-29
BRPI0502597B1 (pt) 2014-12-30
US20120067780A1 (en) 2012-03-22
KR20060049757A (ko) 2006-05-19
DE602005003402T2 (de) 2008-02-28
FR2872516B1 (fr) 2007-03-09
EP1612255B1 (de) 2007-11-21
FR2872516A1 (fr) 2006-01-06
EP1612255B2 (de) 2016-03-30
DK1612255T4 (da) 2016-07-11
US20060000751A1 (en) 2006-01-05
KR101209347B1 (ko) 2012-12-06
BRPI0502597A (pt) 2006-02-14
US8926831B2 (en) 2015-01-06

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8363 Opposition against the patent