EP0321307A2 - Méthode d'isomérisation de cires en huiles lubrifiantes de base - Google Patents
Méthode d'isomérisation de cires en huiles lubrifiantes de base Download PDFInfo
- Publication number
- EP0321307A2 EP0321307A2 EP88311989A EP88311989A EP0321307A2 EP 0321307 A2 EP0321307 A2 EP 0321307A2 EP 88311989 A EP88311989 A EP 88311989A EP 88311989 A EP88311989 A EP 88311989A EP 0321307 A2 EP0321307 A2 EP 0321307A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- wax
- oil
- catalyst
- isomerization
- fraction
- 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.)
- Granted
Links
- 238000000034 method Methods 0.000 title claims abstract description 49
- 239000002199 base oil Substances 0.000 title description 3
- 239000003054 catalyst Substances 0.000 claims abstract description 156
- 239000003921 oil Substances 0.000 claims abstract description 122
- 238000006317 isomerization reaction Methods 0.000 claims abstract description 60
- 238000009835 boiling Methods 0.000 claims abstract description 33
- 239000002904 solvent Substances 0.000 claims abstract description 33
- 238000006243 chemical reaction Methods 0.000 claims abstract description 32
- 230000008569 process Effects 0.000 claims abstract description 28
- 229910052751 metal Inorganic materials 0.000 claims abstract description 27
- 239000002184 metal Substances 0.000 claims abstract description 27
- NTIZESTWPVYFNL-UHFFFAOYSA-N Methyl isobutyl ketone Chemical compound CC(C)CC(C)=O NTIZESTWPVYFNL-UHFFFAOYSA-N 0.000 claims abstract description 15
- 239000010687 lubricating oil Substances 0.000 claims abstract description 13
- 229910044991 metal oxide Inorganic materials 0.000 claims abstract description 5
- 150000004706 metal oxides Chemical class 0.000 claims abstract description 5
- 239000003870 refractory metal Substances 0.000 claims abstract description 5
- 238000002156 mixing Methods 0.000 claims abstract description 4
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 31
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 claims description 20
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 16
- 239000000203 mixture Substances 0.000 claims description 13
- 239000007789 gas Substances 0.000 claims description 9
- 229910052757 nitrogen Inorganic materials 0.000 claims description 9
- 229910052717 sulfur Inorganic materials 0.000 claims description 8
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 6
- 239000011593 sulfur Substances 0.000 claims description 6
- 229930195733 hydrocarbon Natural products 0.000 claims description 5
- 150000002430 hydrocarbons Chemical class 0.000 claims description 5
- 150000002576 ketones Chemical class 0.000 claims description 5
- UIHCLUNTQKBZGK-UHFFFAOYSA-N Methyl isobutyl ketone Natural products CCC(C)C(C)=O UIHCLUNTQKBZGK-UHFFFAOYSA-N 0.000 claims description 4
- 150000004945 aromatic hydrocarbons Chemical class 0.000 claims description 3
- 229940043265 methyl isobutyl ketone Drugs 0.000 claims 2
- 239000001993 wax Substances 0.000 abstract description 152
- 125000005842 heteroatom Chemical group 0.000 abstract description 7
- 150000001491 aromatic compounds Chemical class 0.000 abstract 1
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Substances [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 27
- 239000000047 product Substances 0.000 description 25
- 229910052731 fluorine Inorganic materials 0.000 description 23
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 20
- 230000004913 activation Effects 0.000 description 20
- 239000011737 fluorine Substances 0.000 description 20
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 17
- 239000000463 material Substances 0.000 description 15
- 239000001257 hydrogen Substances 0.000 description 14
- 229910052739 hydrogen Inorganic materials 0.000 description 14
- 239000002245 particle Substances 0.000 description 14
- 238000010438 heat treatment Methods 0.000 description 13
- 229910052697 platinum Inorganic materials 0.000 description 13
- LDDQLRUQCUTJBB-UHFFFAOYSA-N ammonium fluoride Chemical compound [NH4+].[F-] LDDQLRUQCUTJBB-UHFFFAOYSA-N 0.000 description 12
- 239000000243 solution Substances 0.000 description 12
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 description 10
- JKQCZAKAXNWFFN-UHFFFAOYSA-N butan-2-one;4-methylpentan-2-one Chemical compound CCC(C)=O.CC(C)CC(C)=O JKQCZAKAXNWFFN-UHFFFAOYSA-N 0.000 description 10
- 239000000446 fuel Substances 0.000 description 10
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 9
- 238000005194 fractionation Methods 0.000 description 9
- 239000000523 sample Substances 0.000 description 9
- 238000004833 X-ray photoelectron spectroscopy Methods 0.000 description 8
- 238000010790 dilution Methods 0.000 description 8
- 239000012895 dilution Substances 0.000 description 8
- 238000002485 combustion reaction Methods 0.000 description 5
- 238000007689 inspection Methods 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 230000008033 biological extinction Effects 0.000 description 4
- 238000001035 drying Methods 0.000 description 4
- 238000001914 filtration Methods 0.000 description 4
- 238000005984 hydrogenation reaction Methods 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 229910001868 water Inorganic materials 0.000 description 4
- 239000004215 Carbon black (E152) Substances 0.000 description 3
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 239000000460 chlorine Substances 0.000 description 3
- 229910052801 chlorine Inorganic materials 0.000 description 3
- 238000000151 deposition Methods 0.000 description 3
- 238000004821 distillation Methods 0.000 description 3
- 238000007654 immersion Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 238000002791 soaking Methods 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- 238000002441 X-ray diffraction Methods 0.000 description 2
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- WPYMKLBDIGXBTP-UHFFFAOYSA-N benzoic acid Chemical compound OC(=O)C1=CC=CC=C1 WPYMKLBDIGXBTP-UHFFFAOYSA-N 0.000 description 2
- 238000011088 calibration curve Methods 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 239000000356 contaminant Substances 0.000 description 2
- 229910052593 corundum Inorganic materials 0.000 description 2
- 230000001627 detrimental effect Effects 0.000 description 2
- ZZUFCTLCJUWOSV-UHFFFAOYSA-N furosemide Chemical compound C1=C(Cl)C(S(=O)(=O)N)=CC(C(O)=O)=C1NCC1=CC=CO1 ZZUFCTLCJUWOSV-UHFFFAOYSA-N 0.000 description 2
- 230000026030 halogenation Effects 0.000 description 2
- 238000005658 halogenation reaction Methods 0.000 description 2
- 239000012263 liquid product Substances 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 229910052759 nickel Inorganic materials 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 238000004513 sizing Methods 0.000 description 2
- 238000010998 test method Methods 0.000 description 2
- 230000007704 transition Effects 0.000 description 2
- 229910001845 yogo sapphire Inorganic materials 0.000 description 2
- 206010001497 Agitation Diseases 0.000 description 1
- 239000005711 Benzoic acid Substances 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- XZMCDFZZKTWFGF-UHFFFAOYSA-N Cyanamide Chemical compound NC#N XZMCDFZZKTWFGF-UHFFFAOYSA-N 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 229910003638 H2SiF6 Inorganic materials 0.000 description 1
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 150000001450 anions Chemical class 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 235000010233 benzoic acid Nutrition 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000001273 butane Substances 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 239000002775 capsule Substances 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000004587 chromatography analysis Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000012937 correction Methods 0.000 description 1
- 230000009849 deactivation Effects 0.000 description 1
- 239000008367 deionised water Substances 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000001747 exhibiting effect Effects 0.000 description 1
- 150000002222 fluorine compounds Chemical class 0.000 description 1
- 239000000727 fraction Substances 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 150000002367 halogens Chemical class 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 229910052740 iodine Inorganic materials 0.000 description 1
- 238000004255 ion exchange chromatography Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000005453 ketone based solvent Substances 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 238000005007 materials handling Methods 0.000 description 1
- 239000004200 microcrystalline wax Substances 0.000 description 1
- 239000002480 mineral oil Substances 0.000 description 1
- 235000010446 mineral oil Nutrition 0.000 description 1
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 1
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- 239000010453 quartz Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 238000012552 review Methods 0.000 description 1
- 239000012488 sample solution Substances 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- 238000004611 spectroscopical analysis Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000010421 standard material Substances 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- ZEFWRWWINDLIIV-UHFFFAOYSA-N tetrafluorosilane;dihydrofluoride Chemical compound F.F.F[Si](F)(F)F ZEFWRWWINDLIIV-UHFFFAOYSA-N 0.000 description 1
- 125000000383 tetramethylene group Chemical group [H]C([H])([*:1])C([H])([H])C([H])([H])C([H])([H])[*:2] 0.000 description 1
Images
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
- C10G67/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only
- C10G67/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only
- C10G67/04—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only including solvent extraction as the refining step in the absence of hydrogen
Definitions
- Another preferred catalyst is a catalyst prepared by a process involving depositing a hydrogenation metal on an alumina or material containing alumina support, calcining said metal loaded support typically at between 350 to 500°C, preferably about 450 to 500°C for about 1 to 5 hrs, preferably about 1 to 3 hrs and fluoriding said metal loaded support using a high pH fluorine source solution to a bulk fluorine level of about 8 wt% or less (e.g., 2 to 8 wt%), preferably about 7 wt% or less, said high pH source solution being at a pH of 3.5 to 4.5 and preferably being a mixture of NH4F and HF followed by rapid drying/heating in a thin bed or rotary kiln to insure thorough even heating in air, oxygen containing atmosphere or an inert atmosphere to a temperature between about 350 to 450°C in about 3 hours or less, preferably 375 to 400°C and holding at the final temperature, if necessary, for a time sufficient to reduce
- catalysts prepared using solutions of pH 3.5 or less are not heated first, then it is preferred that they be subsequently activated at more severe conditions, i.e. for longer times and/or at higher temperatures. On the other hand, if they are heated first, then moderate activation procedures similar to those employed with catalysts made from the higher pH solution treatment will suffice.
- the sized material will range in size between about 1/64 to 1/32 inch in size.
- the total liquid product (TLP) from the isomerization unit can be advantageously treated in a second stage at mild conditions using the isomerization catalyst or simply noble Group VIII on refractory metal oxide catalyst to reduce PNA and other contaminants in the isomerate and thus yield an oil of improved daylight stability.
- the sample of Catalyst 2 as charged to the 3600 cc unit was activated as follows: at 300 psi H2 at 11 SCF H2/hour per pound of catalyst, heat from room temperature to 100°C at 10°C/hour; hold at 100°C for 24 hours; heat from 100°C to 250°C at 10°C per hour; hold at 250°C for 15 hours; then at 22 SCF H2/hour per pound of catalyst, heat from 250 to 400°C in 31 hours; hold at 400°C for 3 hours.
- Catalyst 5 was prepared by meshing the dried/heated form of Catalyst 5 to a particle size of 1/30" (14/35 mesh). After meshing to a particle size of 1/30" (14/35 mesh), Catalyst 6 was activated in flowing hydrogen by heating from room temperature to 100°C over a 2 hour period, holding at 100°C for 1 hour, heating from 100 to 450°C over a 3 hour period, holding at 450°C for 1 hour. Activation pressure was 50 PSI.
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)
- Lubricants (AREA)
- Catalysts (AREA)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US13515087A | 1987-12-18 | 1987-12-18 | |
US135150 | 1993-10-12 |
Publications (3)
Publication Number | Publication Date |
---|---|
EP0321307A2 true EP0321307A2 (fr) | 1989-06-21 |
EP0321307A3 EP0321307A3 (en) | 1989-08-30 |
EP0321307B1 EP0321307B1 (fr) | 1993-04-21 |
Family
ID=22466775
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP88311989A Expired - Lifetime EP0321307B1 (fr) | 1987-12-18 | 1988-12-16 | Méthode d'isomérisation de cires en huiles lubrifiantes de base |
Country Status (7)
Country | Link |
---|---|
EP (1) | EP0321307B1 (fr) |
JP (1) | JP2607284B2 (fr) |
AU (1) | AU610312B2 (fr) |
CA (1) | CA1333057C (fr) |
DE (1) | DE3880455T2 (fr) |
ES (1) | ES2054835T3 (fr) |
MX (1) | MX169698B (fr) |
Cited By (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0491536A1 (fr) * | 1990-12-19 | 1992-06-24 | Exxon Research And Engineering Company | Isomère de cire ayant un point d'écoulement réduit |
US5275719A (en) * | 1992-06-08 | 1994-01-04 | Mobil Oil Corporation | Production of high viscosity index lubricants |
EP0620264A2 (fr) * | 1993-04-14 | 1994-10-19 | BP Chemicals Limited | Huiles en lubrification |
WO1995007960A1 (fr) * | 1993-09-13 | 1995-03-23 | Exxon Research And Engineering Company | Concentre d'additif utilise avec des essences |
FR2718145A1 (fr) * | 1994-04-01 | 1995-10-06 | Inst Francais Du Petrole | Procédé de traitement avec hydroisomérisation de charges issues du procédé fischer-tropsch. |
FR2718146A1 (fr) * | 1994-04-01 | 1995-10-06 | Inst Francais Du Petrole | Procédé de production d'huiles à partir de coupes lourdes en deux étapes comprenant un hydrotraitement suivi d'une hydroisomérisation. |
WO1997021788A1 (fr) * | 1995-12-08 | 1997-06-19 | Exxon Research And Engineering Company | Huiles de base hydrocarbonees biodegradables et extremement efficaces |
US6103101A (en) * | 1993-10-01 | 2000-08-15 | Petroleo Brasileiro S.A.-Petrobras | Process for producing lube base oils of high viscosity index and diesel oil of high cetaned number |
EP1054942A1 (fr) * | 1998-02-13 | 2000-11-29 | ExxonMobil Research and Engineering Company | Production de lubrifiants a l'aide d'un systeme catalyseur combine |
EP1062305A1 (fr) * | 1998-02-13 | 2000-12-27 | ExxonMobil Research and Engineering Company | Huile de base a faible viscosite pour lubrifiants |
AU730150B2 (en) * | 1997-10-09 | 2001-03-01 | Agip Petroli S.P.A. | Process for the hydroisomerization of long-chain N-paraffins and catalyst suitable for the purpose |
US6420618B1 (en) | 1998-09-04 | 2002-07-16 | Exxonmobil Research And Engineering Company | Premium synthetic lubricant base stock (Law734) having at least 95% noncyclic isoparaffins |
US6475960B1 (en) | 1998-09-04 | 2002-11-05 | Exxonmobil Research And Engineering Co. | Premium synthetic lubricants |
EP1559769A1 (fr) * | 2003-12-19 | 2005-08-03 | Shell Internationale Researchmaatschappij B.V. | Procédé pour la préparation d'huiles de base ayant différents indices de viscosité |
US6962651B2 (en) | 2003-03-10 | 2005-11-08 | Chevron U.S.A. Inc. | Method for producing a plurality of lubricant base oils from paraffinic feedstock |
US7198710B2 (en) | 2003-03-10 | 2007-04-03 | Chevron U.S.A. Inc. | Isomerization/dehazing process for base oils from Fischer-Tropsch wax |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
MY139353A (en) * | 2001-03-05 | 2009-09-30 | Shell Int Research | Process to prepare a lubricating base oil and a gas oil |
CN101198675A (zh) * | 2005-06-23 | 2008-06-11 | 国际壳牌研究有限公司 | 降低蜡质链烷烃类原料的倾点的方法 |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BE627517A (fr) * | 1962-01-26 | |||
US2668866A (en) * | 1951-08-14 | 1954-02-09 | Shell Dev | Isomerization of paraffin wax |
FR1457131A (fr) * | 1964-12-08 | 1966-10-28 | Shell Int Research | Procédé de production d'huiles lubrifiantes ou de constituants d'huiles lubrifiantes |
-
1988
- 1988-12-16 CA CA 586204 patent/CA1333057C/fr not_active Expired - Fee Related
- 1988-12-16 ES ES88311989T patent/ES2054835T3/es not_active Expired - Lifetime
- 1988-12-16 EP EP88311989A patent/EP0321307B1/fr not_active Expired - Lifetime
- 1988-12-16 DE DE19883880455 patent/DE3880455T2/de not_active Expired - Fee Related
- 1988-12-16 MX MX1423388A patent/MX169698B/es unknown
- 1988-12-16 AU AU26940/88A patent/AU610312B2/en not_active Ceased
- 1988-12-19 JP JP63320306A patent/JP2607284B2/ja not_active Expired - Fee Related
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2668866A (en) * | 1951-08-14 | 1954-02-09 | Shell Dev | Isomerization of paraffin wax |
BE627517A (fr) * | 1962-01-26 | |||
FR1457131A (fr) * | 1964-12-08 | 1966-10-28 | Shell Int Research | Procédé de production d'huiles lubrifiantes ou de constituants d'huiles lubrifiantes |
Cited By (27)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0491536A1 (fr) * | 1990-12-19 | 1992-06-24 | Exxon Research And Engineering Company | Isomère de cire ayant un point d'écoulement réduit |
US5149452A (en) * | 1990-12-19 | 1992-09-22 | Exxon Research And Engineering Company | Wax isomerate having a reduced pour point |
US5275719A (en) * | 1992-06-08 | 1994-01-04 | Mobil Oil Corporation | Production of high viscosity index lubricants |
EP0620264A2 (fr) * | 1993-04-14 | 1994-10-19 | BP Chemicals Limited | Huiles en lubrification |
EP0620264A3 (fr) * | 1993-04-14 | 1995-02-08 | Bp Chem Int Ltd | Huiles en lubrification. |
WO1995007960A1 (fr) * | 1993-09-13 | 1995-03-23 | Exxon Research And Engineering Company | Concentre d'additif utilise avec des essences |
US5720782A (en) * | 1993-09-13 | 1998-02-24 | Exxon Research And Engineering Company | Additive concentrate for use with gasolines |
US6103101A (en) * | 1993-10-01 | 2000-08-15 | Petroleo Brasileiro S.A.-Petrobras | Process for producing lube base oils of high viscosity index and diesel oil of high cetaned number |
FR2718145A1 (fr) * | 1994-04-01 | 1995-10-06 | Inst Francais Du Petrole | Procédé de traitement avec hydroisomérisation de charges issues du procédé fischer-tropsch. |
FR2718146A1 (fr) * | 1994-04-01 | 1995-10-06 | Inst Francais Du Petrole | Procédé de production d'huiles à partir de coupes lourdes en deux étapes comprenant un hydrotraitement suivi d'une hydroisomérisation. |
WO1995027020A1 (fr) * | 1994-04-01 | 1995-10-12 | Institut Français Du Petrole | Procede de traitement avec hydroisomerisation de charges issues du procede fischer-tropsch |
US5834522A (en) * | 1994-04-01 | 1998-11-10 | Institut Francais Du Petrole | Hydroisomerization treatment process for feeds from the fisher-tropsch process |
US6096940A (en) * | 1995-12-08 | 2000-08-01 | Exxon Research And Engineering Company | Biodegradable high performance hydrocarbon base oils |
WO1997021788A1 (fr) * | 1995-12-08 | 1997-06-19 | Exxon Research And Engineering Company | Huiles de base hydrocarbonees biodegradables et extremement efficaces |
EP1389635A1 (fr) * | 1995-12-08 | 2004-02-18 | ExxonMobil Research and Engineering Company | Huiles de base hydrocarburées à haute performance. |
US6506297B1 (en) | 1995-12-08 | 2003-01-14 | Exxonmobile Research And Engineering Company | Biodegradable high performance hydrocarbon base oils |
AU730150B2 (en) * | 1997-10-09 | 2001-03-01 | Agip Petroli S.P.A. | Process for the hydroisomerization of long-chain N-paraffins and catalyst suitable for the purpose |
EP1062305A1 (fr) * | 1998-02-13 | 2000-12-27 | ExxonMobil Research and Engineering Company | Huile de base a faible viscosite pour lubrifiants |
EP1054942A1 (fr) * | 1998-02-13 | 2000-11-29 | ExxonMobil Research and Engineering Company | Production de lubrifiants a l'aide d'un systeme catalyseur combine |
EP1062305A4 (fr) * | 1998-02-13 | 2005-03-09 | Exxonmobil Res & Eng Co | Huile de base a faible viscosite pour lubrifiants |
EP1054942A4 (fr) * | 1998-02-13 | 2006-07-26 | Exxonmobil Res & Eng Co | Production de lubrifiants a l'aide d'un systeme catalyseur combine |
US6420618B1 (en) | 1998-09-04 | 2002-07-16 | Exxonmobil Research And Engineering Company | Premium synthetic lubricant base stock (Law734) having at least 95% noncyclic isoparaffins |
US6475960B1 (en) | 1998-09-04 | 2002-11-05 | Exxonmobil Research And Engineering Co. | Premium synthetic lubricants |
US6962651B2 (en) | 2003-03-10 | 2005-11-08 | Chevron U.S.A. Inc. | Method for producing a plurality of lubricant base oils from paraffinic feedstock |
US7198710B2 (en) | 2003-03-10 | 2007-04-03 | Chevron U.S.A. Inc. | Isomerization/dehazing process for base oils from Fischer-Tropsch wax |
NL1025687C2 (nl) * | 2003-03-10 | 2010-05-18 | Chevron Usa Inc | Werkwijze voor het produceren van een veelheid van smeermiddelbasisoliën uit een paraffinische voeding. |
EP1559769A1 (fr) * | 2003-12-19 | 2005-08-03 | Shell Internationale Researchmaatschappij B.V. | Procédé pour la préparation d'huiles de base ayant différents indices de viscosité |
Also Published As
Publication number | Publication date |
---|---|
MX169698B (es) | 1993-07-19 |
DE3880455D1 (de) | 1993-05-27 |
JPH01301788A (ja) | 1989-12-05 |
EP0321307B1 (fr) | 1993-04-21 |
JP2607284B2 (ja) | 1997-05-07 |
AU2694088A (en) | 1989-06-22 |
ES2054835T3 (es) | 1994-08-16 |
AU610312B2 (en) | 1991-05-16 |
EP0321307A3 (en) | 1989-08-30 |
DE3880455T2 (de) | 1993-09-16 |
CA1333057C (fr) | 1994-11-15 |
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