NO20022640D0 - Naftaavsvovling ved höy temperatur ved bruk av en lite metallholdig og delvis desaktivitert katalysator - Google Patents
Naftaavsvovling ved höy temperatur ved bruk av en lite metallholdig og delvis desaktivitert katalysatorInfo
- Publication number
- NO20022640D0 NO20022640D0 NO20022640A NO20022640A NO20022640D0 NO 20022640 D0 NO20022640 D0 NO 20022640D0 NO 20022640 A NO20022640 A NO 20022640A NO 20022640 A NO20022640 A NO 20022640A NO 20022640 D0 NO20022640 D0 NO 20022640D0
- Authority
- NO
- Norway
- Prior art keywords
- desulphurization
- naphtha
- high temperature
- small metal
- deactivated catalyst
- Prior art date
Links
- 239000003054 catalyst Substances 0.000 title 1
- 239000002184 metal Substances 0.000 title 1
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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/85—Chromium, molybdenum or tungsten
- B01J23/88—Molybdenum
- B01J23/882—Molybdenum and cobalt
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/30—Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
- B01J35/396—Distribution of the active metal ingredient
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/40—Catalysts, in general, characterised by their form or physical properties characterised by dimensions, e.g. grain size
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/64—Pore diameter
- B01J35/647—2-50 nm
-
- 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
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/02—Gasoline
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Materials Engineering (AREA)
- General Chemical & Material Sciences (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Catalysts (AREA)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US09/455,885 US6231754B1 (en) | 1996-02-02 | 1999-12-06 | High temperature naphtha desulfurization using a low metal and partially deactivated catalyst |
PCT/US2000/035703 WO2001072929A1 (fr) | 1999-12-06 | 2000-12-05 | Desulfuration de naphte haute temperature employant un catalyseur partiellement desactive a faible teneur en metaux |
Publications (2)
Publication Number | Publication Date |
---|---|
NO20022640L NO20022640L (no) | 2002-06-04 |
NO20022640D0 true NO20022640D0 (no) | 2002-06-04 |
Family
ID=23810639
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
NO20022640A NO20022640D0 (no) | 1999-12-06 | 2002-06-04 | Naftaavsvovling ved höy temperatur ved bruk av en lite metallholdig og delvis desaktivitert katalysator |
Country Status (7)
Country | Link |
---|---|
US (1) | US6231754B1 (fr) |
EP (1) | EP1246891A4 (fr) |
JP (1) | JP2003528972A (fr) |
AU (1) | AU773870B2 (fr) |
CA (1) | CA2389471A1 (fr) |
NO (1) | NO20022640D0 (fr) |
WO (1) | WO2001072929A1 (fr) |
Families Citing this family (29)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6893554B2 (en) * | 2002-03-13 | 2005-05-17 | Exxonmobil Research And Engineering Company | Naphtha desulfurization with selectively suppressed hydrogenation |
US7074735B2 (en) * | 2002-03-13 | 2006-07-11 | Exxonmobil Research And Engineering Company | Selectively suppressing catalytic hydrogenation |
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 |
US7422679B2 (en) * | 2002-05-28 | 2008-09-09 | Exxonmobil Research And Engineering Company | Low CO for increased naphtha desulfurization |
US7074324B2 (en) * | 2002-06-05 | 2006-07-11 | Exxonmobil Research And Engineering Company | Process to remove sulfur contaminants from hydrocarbon streams |
US7297252B2 (en) | 2003-01-13 | 2007-11-20 | Exxonmobil Research And Engineering Company | Catalyst activation in the presence of olefinic hydrocarbon for selective naphtha hydrodesulfurization |
US7629289B2 (en) * | 2004-06-23 | 2009-12-08 | Uop Llc | Selective naphtha desulfurization process and catalyst |
FR2872516B1 (fr) | 2004-07-01 | 2007-03-09 | Inst Francais Du Petrole | Procede d'hydrodesulfuration des essences mettant en oeuvre un catalyseur a porosite controlee |
US7473350B2 (en) * | 2005-01-13 | 2009-01-06 | China Petroleum & Chemical Corporation | Control methodology for desulfurization process |
FR2888583B1 (fr) * | 2005-07-18 | 2007-09-28 | Inst Francais Du Petrole | Nouveau procede de desulfuration d'essences olefiniques permettant de limiter la teneur en mercaptans |
CN1325419C (zh) * | 2005-12-19 | 2007-07-11 | 北京朗新明环保科技有限公司 | 烟气脱硫石膏浆液的脱水方法及装置 |
BRPI0601787B1 (pt) | 2006-05-17 | 2016-06-07 | Petroleo Brasileiro Sa | processo de hidrodessulfurização seletiva de nafta |
US20080093265A1 (en) * | 2006-10-18 | 2008-04-24 | Exxonmobil Research And Engineering Company | Process for selective sulfur removal from FCC naphthas using zeolite catalysts |
US7837861B2 (en) * | 2006-10-18 | 2010-11-23 | Exxonmobil Research & Engineering Co. | Process for benzene reduction and sulfur removal from FCC naphthas |
DE102006060950A1 (de) * | 2006-12-20 | 2008-07-03 | Forschungszentrum Jülich GmbH | Verfahren zur Reinigung von Mineralölfraktionen sowie zur Durchführung des Verfahrens geeignete Vorrichtung |
CN101508909B (zh) * | 2009-03-19 | 2012-05-30 | 中国石油大学(北京) | 劣质汽油选择性加氢脱硫与多支链异构的耦合改质方法 |
WO2011031828A2 (fr) * | 2009-09-11 | 2011-03-17 | Exxonmobil Research And Engineering Company | Désulfuration sélective du naphta à l'aide d'inhibiteurs de réaction |
US8894844B2 (en) | 2011-03-21 | 2014-11-25 | Exxonmobil Research And Engineering Company | Hydroprocessing methods utilizing carbon oxide-tolerant catalysts |
CN103381374B (zh) * | 2013-03-03 | 2015-11-11 | 曹学仁 | 一种催化剂保护剂填料的制备方法 |
US9850435B2 (en) | 2014-08-26 | 2017-12-26 | Exxonmobil Research And Engineering Company | Hydroprocessing with drum blanketing gas compositional control |
CA3049804A1 (fr) | 2017-02-21 | 2018-08-30 | Exxonmobil Research And Engineering Company | Desulfuration d'une alimentation d'intervalle de distillation de naphta |
CN110064405B (zh) * | 2018-01-23 | 2022-03-01 | 中国石油天然气股份有限公司 | 一种具有脱硫活性的加氢处理催化剂的制备方法 |
FR3099174B1 (fr) | 2019-07-23 | 2021-11-12 | Ifp Energies Now | Procédé de production d'une essence a basse teneur en soufre et en mercaptans |
FR3099173B1 (fr) | 2019-07-23 | 2021-07-09 | Ifp Energies Now | Procédé de production d'une essence a basse teneur en soufre et en mercaptans |
FR3099172B1 (fr) | 2019-07-23 | 2021-07-16 | Ifp Energies Now | Procede de traitement d'une essence par separation en trois coupes |
FR3099175B1 (fr) | 2019-07-23 | 2021-07-16 | Ifp Energies Now | Procédé de production d'une essence a basse teneur en soufre et en mercaptans |
FR3108333B1 (fr) | 2020-03-20 | 2022-03-11 | Ifp Energies Now | Procédé de production d'une essence a basse teneur en soufre et en mercaptans |
FR3130831A1 (fr) | 2021-12-20 | 2023-06-23 | IFP Energies Nouvelles | Procédé de production d'une coupe essence légère à basse teneur en soufre |
FR3130834A1 (fr) | 2021-12-20 | 2023-06-23 | IFP Energies Nouvelles | Procédé de traitement d'une essence contenant des composés soufrés |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3809644A (en) * | 1972-08-01 | 1974-05-07 | Hydrocarbon Research Inc | Multiple stage hydrodesulfurization of residuum |
US3870626A (en) * | 1973-02-27 | 1975-03-11 | Gulf Research Development Co | Method for reducing the mercaptan content of a middle distillate oil |
US4016067A (en) * | 1975-02-21 | 1977-04-05 | Mobil Oil Corporation | Process for demetalation and desulfurization of petroleum oils |
US4149965A (en) | 1978-06-27 | 1979-04-17 | Exxon Research & Engineering Co. | Method for starting-up a naphtha hydrorefining process |
US5423975A (en) | 1992-07-08 | 1995-06-13 | Texaco Inc. | Selective hydrodesulfurization of naphtha using spent resid catalyst |
US5286373A (en) * | 1992-07-08 | 1994-02-15 | Texaco Inc. | Selective hydrodesulfurization of naphtha using deactivated hydrotreating catalyst |
US5525211A (en) | 1994-10-06 | 1996-06-11 | Texaco Inc. | Selective hydrodesulfurization of naphtha using selectively poisoned hydroprocessing catalyst |
JP3387700B2 (ja) | 1995-07-26 | 2003-03-17 | 新日本石油株式会社 | 接触分解ガソリンの脱硫方法 |
US5985136A (en) * | 1998-06-18 | 1999-11-16 | Exxon Research And Engineering Co. | Two stage hydrodesulfurization process |
-
1999
- 1999-12-06 US US09/455,885 patent/US6231754B1/en not_active Expired - Lifetime
-
2000
- 2000-12-05 AU AU26115/01A patent/AU773870B2/en not_active Ceased
- 2000-12-05 EP EP00989629A patent/EP1246891A4/fr not_active Withdrawn
- 2000-12-05 JP JP2001571846A patent/JP2003528972A/ja active Pending
- 2000-12-05 CA CA002389471A patent/CA2389471A1/fr not_active Abandoned
- 2000-12-05 WO PCT/US2000/035703 patent/WO2001072929A1/fr active IP Right Grant
-
2002
- 2002-06-04 NO NO20022640A patent/NO20022640D0/no not_active Application Discontinuation
Also Published As
Publication number | Publication date |
---|---|
WO2001072929A1 (fr) | 2001-10-04 |
AU2611501A (en) | 2001-10-08 |
AU773870B2 (en) | 2004-06-10 |
EP1246891A1 (fr) | 2002-10-09 |
NO20022640L (no) | 2002-06-04 |
JP2003528972A (ja) | 2003-09-30 |
CA2389471A1 (fr) | 2001-10-04 |
EP1246891A4 (fr) | 2004-02-18 |
US6231754B1 (en) | 2001-05-15 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
FC2A | Withdrawal, rejection or dismissal of laid open patent application |