NO20065347L - Process for the manufacture of lubricating oil products - Google Patents
Process for the manufacture of lubricating oil productsInfo
- Publication number
- NO20065347L NO20065347L NO20065347A NO20065347A NO20065347L NO 20065347 L NO20065347 L NO 20065347L NO 20065347 A NO20065347 A NO 20065347A NO 20065347 A NO20065347 A NO 20065347A NO 20065347 L NO20065347 L NO 20065347L
- Authority
- NO
- Norway
- Prior art keywords
- group
- lubricating oil
- mixtures
- component selected
- metal
- 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
- 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
-
- 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
-
- 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
- B01J23/887—Molybdenum containing in addition other metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/8877—Vanadium, tantalum, niobium or polonium
-
- 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
- B01J23/888—Tungsten
-
- 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
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/0009—Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/04—Mixing
Abstract
Den foreliggende oppfinnelsen vedrører en fremgangsmåte for å fremstille smøreoljeprodukter gjennom hydrogenbehandlingen av fødestrømmer med kokeområde for smøreoljer, i nærvær av en bulkmetallhydrogenbehandlingskatalysator omfattende: i: en gruppe VIB-metallkomponent valgt fra molybden, wolfram og blandinger derav; ii: en gruppe V-metallkomponent valgt fra vanadium, niob, tantal og blandinger derav; og en gruppe VIII-metallkomponent valgt fra nikkel, kobolt, jern og blandinger derav, hvori metallkomponentene (kalkulert som oksider) omfatter minst 50 vekt% av katalysatoren, hvori molforholdet mellom metallkomponentene tilfredsstiller formelen (gruppe VIB + gruppe V): (gruppe VIII) = 0,35-2:1. 1The present invention relates to a process for preparing lubricating oil products through the hydrogen treatment of feed streams with a lubricating oil cooking range, in the presence of a bulk metal hydrogen treatment catalyst comprising: in: a group VIB metal component selected from molybdenum, tungsten and mixtures thereof; ii: a Group V metal component selected from vanadium, niobium, tantalum and mixtures thereof; and a Group VIII metal component selected from nickel, cobalt, iron and mixtures thereof, wherein the metal components (calculated as oxides) comprise at least 50% by weight of the catalyst, wherein the molar ratio of the metal components satisfies the formula (Group VIB + Group V): (Group VIII) = 0.35-2: 1. 1
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US56440404P | 2004-04-22 | 2004-04-22 | |
PCT/US2005/012623 WO2005108528A1 (en) | 2004-04-22 | 2005-04-13 | Process to manufacture luge oil products |
Publications (1)
Publication Number | Publication Date |
---|---|
NO20065347L true NO20065347L (en) | 2006-11-22 |
Family
ID=34966350
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
NO20065347A NO20065347L (en) | 2004-04-22 | 2006-11-22 | Process for the manufacture of lubricating oil products |
Country Status (7)
Country | Link |
---|---|
US (1) | US20050236304A1 (en) |
EP (1) | EP1737932A1 (en) |
JP (1) | JP2007533827A (en) |
AU (1) | AU2005241000A1 (en) |
CA (1) | CA2563706A1 (en) |
NO (1) | NO20065347L (en) |
WO (1) | WO2005108528A1 (en) |
Families Citing this family (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2002018043A1 (en) * | 2000-08-28 | 2002-03-07 | Research Triangle Institute | Attrition resistant bulk iron catalysts and processes for preparing and using same |
US7776205B2 (en) * | 2004-04-22 | 2010-08-17 | Exxonmobil Research And Engineering Company | Process to upgrade hydrocarbonaceous feedstreams |
US7780845B2 (en) * | 2004-04-22 | 2010-08-24 | Exxonmobil Research And Engineering Company | Process to manufacture low sulfur distillates |
US7648941B2 (en) * | 2004-09-22 | 2010-01-19 | Exxonmobil Research And Engineering Company | Bulk bimetallic catalysts, method of making bulk bimetallic catalysts and hydroprocessing using bulk bimetallic catalysts |
WO2007050633A2 (en) * | 2005-10-26 | 2007-05-03 | Exxonmobil Research And Engineering Company | Hydroprocessing using bulk bimetallic catalysts |
KR101373988B1 (en) * | 2005-10-26 | 2014-03-12 | 알베마를 네덜란드 비.브이. | A bulk catalyst comprising nickel tungsten metal oxidic particles |
FR2910351B1 (en) * | 2006-12-22 | 2009-02-27 | Total France Sa | HYDROTREATING CATALYST, PROCESS FOR PREPARING THE SAME AND USE THEREOF |
DE102007007325A1 (en) * | 2007-02-14 | 2008-08-21 | Süd-Chemie AG | A catalyst comprising a zeolite and a binder comprising a niobium or tantalum-containing acidic compound |
JP5543361B2 (en) * | 2007-12-04 | 2014-07-09 | アルベマール・ネーザーランズ・ベー・ブイ | Process for preparing bulk metal oxide particles |
CN110038597B (en) * | 2018-01-16 | 2021-12-07 | 中国石油化工股份有限公司 | Preparation method of hydrofining catalyst |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2946738A (en) * | 1957-07-01 | 1960-07-26 | Phillips Petroleum Co | Hydrocracking a gas oil with a presulfided catalyst consisting of oxides of vanadium, cobalt and molybdenum on gamma alumina |
FR2553680B1 (en) * | 1983-10-25 | 1987-09-18 | Inst Francais Du Petrole | CATALYSTS BASED ON GROUP VIII AND GROUP VIB METAL SULFIDES FOR HYDROPROCESSING REACTIONS OF SULFUR-CONTAINING HYDROCARBON CUTS |
US5252199A (en) * | 1990-10-01 | 1993-10-12 | Exxon Research & Engineering Company | Hydrotreating process using novel multimetallic sulfide catalysts |
DE69708829T2 (en) * | 1996-12-27 | 2002-04-04 | Inst Francais Du Petrole | Hydrogen treatment and hydrocracking catalyst containing a mixed sulfide with sulfur, at least one element from group 5B and at least one element from group 6B |
FR2780311B1 (en) * | 1998-06-25 | 2000-08-11 | Inst Francais Du Petrole | HYDROCRACKING CATALYST COMPRISING A NON-GLOBALLY DESALUMINATED Y ZEOLITE, A VB GROUP ELEMENT, AND A PROMOTING ELEMENT SELECTED IN THE GROUP FORMED BY BORON, PHOSPHORUS AND SILICON |
DE69930362T2 (en) * | 1998-06-25 | 2006-12-14 | Institut Français du Pétrole, Rueil-Malmaison | A hydrocleavage catalyst containing a beta zeolite and a Group VB element |
JP5246980B2 (en) * | 1999-01-15 | 2013-07-24 | アルベマーレ ネザーランズ ビー.ブイ. | Mixed metal catalyst composition, process for its production and use |
-
2005
- 2005-04-01 US US11/096,500 patent/US20050236304A1/en not_active Abandoned
- 2005-04-13 EP EP05737817A patent/EP1737932A1/en not_active Withdrawn
- 2005-04-13 CA CA002563706A patent/CA2563706A1/en not_active Abandoned
- 2005-04-13 AU AU2005241000A patent/AU2005241000A1/en not_active Abandoned
- 2005-04-13 WO PCT/US2005/012623 patent/WO2005108528A1/en not_active Application Discontinuation
- 2005-04-13 JP JP2007509521A patent/JP2007533827A/en active Pending
-
2006
- 2006-11-22 NO NO20065347A patent/NO20065347L/en not_active Application Discontinuation
Also Published As
Publication number | Publication date |
---|---|
AU2005241000A1 (en) | 2005-11-17 |
CA2563706A1 (en) | 2005-11-17 |
WO2005108528A1 (en) | 2005-11-17 |
US20050236304A1 (en) | 2005-10-27 |
EP1737932A1 (en) | 2007-01-03 |
JP2007533827A (en) | 2007-11-22 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
FC2A | Withdrawal, rejection or dismissal of laid open patent application |