GB1065205A - Process for the production of lubricating oils or lubricating oil components - Google Patents
Process for the production of lubricating oils or lubricating oil componentsInfo
- Publication number
- GB1065205A GB1065205A GB5159265A GB5159265A GB1065205A GB 1065205 A GB1065205 A GB 1065205A GB 5159265 A GB5159265 A GB 5159265A GB 5159265 A GB5159265 A GB 5159265A GB 1065205 A GB1065205 A GB 1065205A
- Authority
- GB
- United Kingdom
- Prior art keywords
- zone
- wax
- catalyst
- effluent
- alumina
- 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.)
- Expired
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
- C10G45/58—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins
- C10G45/60—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins 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
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/10—Lubricating oil
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Crystallography & Structural Chemistry (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)
Abstract
Lubricating oils or components therefor are produced from petroleum waxes by a process comprising the following steps: (a) isomerizing a petroleum wax in the presence of hydrogen in a first zone over a catalyst containing a hydrogenation/dehydrogenation component and a solid acid-acting refractory support; (b) isomerizing at least the portion boiling in the lubricating oil boiling range of the effluent from the first zone in the presence of hydrogen over a catalyst containing a hydrogenation/dehydrogenation component and a solid acid-acting refractory support in a second zone; (c) separating the portion boiling in the lubricating oil boiling range from the effluent from the second zone; and (d) dewaxing this portion. The wax starting material may be one obtained from a residual oil or a distillate oil, preferably the former, and may be soft wax obtained by de-oiling crude wax. Both isomerization zones may operate under the following conditions: temp. 316-492 DEG C., pressure 35-140 atmospheres absolute, space velocity 0.1-5 litres of wax/hour/litre of catalyst, and hydrogen/wax mole ratio 5-50. The catalyst in each zone may be at least one metal and/or oxide and/or sulphide thereof of Group II, V, VI or VIII of the Periodic Table. Preferably, the catalyst in the first zone is sulphur-resistant, e.g. tungsten and nickel oxides and/or sulphides, and that in the second zone is sulphur-sensitive, e.g. platinum. The support for the catalysts may be silica/alumina/BF3, silica/magnesia, silica/alumina/zirconia, alumina/fluorine, acid-treated clay, montmorillonite clay, a zeolite clay, or a molecular sieve. The effluent from the first zone is preferably fractionated or flashed to remove hydrocarbons boiling below the lube oil range, and the wax from the dewaxing stage (d) may be recycled to the second isomerization zone. The dewaxing stage is conventional, preferably by solvents, e.g. liquid propane, benzene, toluene, methyl ethyl ketone, or toluene/methyl ethyl ketone mixtures. The process gives higher lube oil yields than known single stage processes.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US41689464A | 1964-12-08 | 1964-12-08 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1065205A true GB1065205A (en) | 1967-04-12 |
Family
ID=23651745
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB5159265A Expired GB1065205A (en) | 1964-12-08 | 1965-12-06 | Process for the production of lubricating oils or lubricating oil components |
Country Status (4)
Country | Link |
---|---|
DE (1) | DE1271292B (en) |
FR (1) | FR1457131A (en) |
GB (1) | GB1065205A (en) |
NL (1) | NL149219B (en) |
Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4900707A (en) * | 1987-12-18 | 1990-02-13 | Exxon Research And Engineering Company | Method for producing a wax isomerization catalyst |
US4906601A (en) * | 1988-12-16 | 1990-03-06 | Exxon Research And Engineering Company | Small particle low fluoride content catalyst |
US4923588A (en) * | 1988-12-16 | 1990-05-08 | Exxon Research And Engineering Company | Wax isomerization using small particle low fluoride content catalysts |
US4929795A (en) * | 1987-12-18 | 1990-05-29 | Exxon Research And Engineering Company | Method for isomerizing wax to lube base oils using an isomerization catalyst |
US4937399A (en) * | 1987-12-18 | 1990-06-26 | Exxon Research And Engineering Company | Method for isomerizing wax to lube base oils using a sized isomerization catalyst |
US4959337A (en) * | 1987-12-18 | 1990-09-25 | Exxon Research And Engineering Company | Wax isomerization catalyst and method for its production |
US4992159A (en) * | 1988-12-16 | 1991-02-12 | Exxon Research And Engineering Company | Upgrading waxy distillates and raffinates by the process of hydrotreating and hydroisomerization |
US5059299A (en) * | 1987-12-18 | 1991-10-22 | Exxon Research And Engineering Company | Method for isomerizing wax to lube base oils |
US5158671A (en) * | 1987-12-18 | 1992-10-27 | Exxon Research And Engineering Company | Method for stabilizing hydroisomerates |
EP0537969A2 (en) * | 1991-10-18 | 1993-04-21 | Texaco Development Corporation | Wax conversion process |
EP0710710A2 (en) * | 1994-11-01 | 1996-05-08 | Exxon Research And Engineering Company | Catalyst combination for improved wax isomerization |
AU716981B2 (en) * | 1996-02-02 | 2000-03-16 | Exxon Research And Engineering Company | Hydroisomerization with reduced hydrocracking |
US6274029B1 (en) | 1995-10-17 | 2001-08-14 | Exxon Research And Engineering Company | Synthetic diesel fuel and process for its production |
US6309432B1 (en) | 1997-02-07 | 2001-10-30 | Exxon Research And Engineering Company | Synthetic jet fuel and process for its production |
US6822131B1 (en) | 1995-10-17 | 2004-11-23 | Exxonmobil Reasearch And Engineering Company | Synthetic diesel fuel and process for its production |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2194767B1 (en) * | 1972-08-04 | 1975-03-07 | Shell France | |
FR2124138A2 (en) * | 1971-02-09 | 1972-09-22 | Shell Berre Raffinage | Lubricating oils of very high viscosity index - by hydrocracking followed by deparaffination and paraffin hydroisomerization |
AU610312B2 (en) * | 1987-12-18 | 1991-05-16 | Exxon Research And Engineering Company | Method for isomerizing wax to lube base oils |
FR2676749B1 (en) * | 1991-05-21 | 1993-08-20 | Inst Francais Du Petrole | PROCESS FOR HYDROISOMERIZATION OF PARAFFINS FROM THE FISCHER-TROPSCH PROCESS USING H-Y ZEOLITE CATALYSTS. |
US6383366B1 (en) * | 1998-02-13 | 2002-05-07 | Exxon Research And Engineering Company | Wax hydroisomerization process |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BE537743A (en) * | ||||
FR659631A (en) * | 1927-09-09 | 1929-07-01 | Landis & Gyr Sa | Device for modifying the temperature coefficient of electrical measuring instruments based on the induction principle |
BE497757A (en) * | 1949-10-17 | |||
DE931826C (en) * | 1951-08-14 | 1955-08-18 | Bataafsche Petroleum | Process for isomerizing paraffin |
FR1068757A (en) * | 1951-08-14 | 1954-06-30 | Bataafsche Petroleum | Paraffin isomerization process |
DE1033193B (en) * | 1953-03-31 | 1958-07-03 | Bataafsche Petroleum | Process for the catalytic isomerization of solid, paraffin-containing hydrocarbons |
-
1965
- 1965-12-06 GB GB5159265A patent/GB1065205A/en not_active Expired
- 1965-12-06 FR FR41097A patent/FR1457131A/en not_active Expired
- 1965-12-06 DE DEP1271A patent/DE1271292B/en active Pending
- 1965-12-07 NL NL6515853A patent/NL149219B/en not_active IP Right Cessation
Cited By (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4900707A (en) * | 1987-12-18 | 1990-02-13 | Exxon Research And Engineering Company | Method for producing a wax isomerization catalyst |
US4929795A (en) * | 1987-12-18 | 1990-05-29 | Exxon Research And Engineering Company | Method for isomerizing wax to lube base oils using an isomerization catalyst |
US4937399A (en) * | 1987-12-18 | 1990-06-26 | Exxon Research And Engineering Company | Method for isomerizing wax to lube base oils using a sized isomerization catalyst |
US4959337A (en) * | 1987-12-18 | 1990-09-25 | Exxon Research And Engineering Company | Wax isomerization catalyst and method for its production |
US5059299A (en) * | 1987-12-18 | 1991-10-22 | Exxon Research And Engineering Company | Method for isomerizing wax to lube base oils |
US5158671A (en) * | 1987-12-18 | 1992-10-27 | Exxon Research And Engineering Company | Method for stabilizing hydroisomerates |
US4906601A (en) * | 1988-12-16 | 1990-03-06 | Exxon Research And Engineering Company | Small particle low fluoride content catalyst |
US4923588A (en) * | 1988-12-16 | 1990-05-08 | Exxon Research And Engineering Company | Wax isomerization using small particle low fluoride content catalysts |
US4992159A (en) * | 1988-12-16 | 1991-02-12 | Exxon Research And Engineering Company | Upgrading waxy distillates and raffinates by the process of hydrotreating and hydroisomerization |
EP0537969A3 (en) * | 1991-10-18 | 1993-06-16 | Texaco Development Corporation | Wax conversion process |
EP0537969A2 (en) * | 1991-10-18 | 1993-04-21 | Texaco Development Corporation | Wax conversion process |
EP0710710A2 (en) * | 1994-11-01 | 1996-05-08 | Exxon Research And Engineering Company | Catalyst combination for improved wax isomerization |
EP0710710A3 (en) * | 1994-11-01 | 1996-07-03 | Exxon Research Engineering Co | Catalyst combination for improved wax isomerization |
US6274029B1 (en) | 1995-10-17 | 2001-08-14 | Exxon Research And Engineering Company | Synthetic diesel fuel and process for its production |
US6296757B1 (en) | 1995-10-17 | 2001-10-02 | Exxon Research And Engineering Company | Synthetic diesel fuel and process for its production |
US6607568B2 (en) | 1995-10-17 | 2003-08-19 | Exxonmobil Research And Engineering Company | Synthetic diesel fuel and process for its production (law3 1 1) |
US6822131B1 (en) | 1995-10-17 | 2004-11-23 | Exxonmobil Reasearch And Engineering Company | Synthetic diesel fuel and process for its production |
AU716981B2 (en) * | 1996-02-02 | 2000-03-16 | Exxon Research And Engineering Company | Hydroisomerization with reduced hydrocracking |
US6309432B1 (en) | 1997-02-07 | 2001-10-30 | Exxon Research And Engineering Company | Synthetic jet fuel and process for its production |
US6669743B2 (en) | 1997-02-07 | 2003-12-30 | Exxonmobil Research And Engineering Company | Synthetic jet fuel and process for its production (law724) |
Also Published As
Publication number | Publication date |
---|---|
FR1457131A (en) | 1966-10-28 |
NL6515853A (en) | 1966-06-09 |
DE1271292B (en) | 1968-06-27 |
NL149219B (en) | 1976-04-15 |
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