DK1612255T3 - Afsvovlingsfremgangsmåde til naphtafraktionen, der anvender en katalysator med styret porösitet - Google Patents
Afsvovlingsfremgangsmåde til naphtafraktionen, der anvender en katalysator med styret porösitetInfo
- 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
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
- 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
-
- 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
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)
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)
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)
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 |
-
2004
- 2004-07-01 FR FR0407335A patent/FR2872516B1/fr active Active
-
2005
- 2005-06-27 DE DE602005003402.1T patent/DE602005003402T3/de active Active
- 2005-06-27 EP EP05291383.7A patent/EP1612255B2/fr active Active
- 2005-06-27 DK DK05291383.7T patent/DK1612255T4/da active
- 2005-06-28 CA CA2510668A patent/CA2510668C/fr active Active
- 2005-06-29 BR BRPI0502597-4A patent/BRPI0502597B1/pt active IP Right Grant
- 2005-07-01 US US11/171,287 patent/US20060000751A1/en not_active Abandoned
- 2005-07-01 KR KR1020050059196A patent/KR101209347B1/ko active IP Right Grant
-
2011
- 2011-11-28 US US13/305,527 patent/US8926831B2/en active Active
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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