EP2504416A1 - Additive concentrate - Google Patents
Additive concentrateInfo
- Publication number
- EP2504416A1 EP2504416A1 EP10784756A EP10784756A EP2504416A1 EP 2504416 A1 EP2504416 A1 EP 2504416A1 EP 10784756 A EP10784756 A EP 10784756A EP 10784756 A EP10784756 A EP 10784756A EP 2504416 A1 EP2504416 A1 EP 2504416A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- additive concentrate
- base oil
- astm
- fischer
- additive
- 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.)
- Withdrawn
Links
- 239000000654 additive Substances 0.000 title claims abstract description 111
- 230000000996 additive effect Effects 0.000 title claims abstract description 98
- 239000012141 concentrate Substances 0.000 title claims abstract description 93
- 239000002199 base oil Substances 0.000 claims abstract description 70
- 239000004034 viscosity adjusting agent Substances 0.000 claims abstract description 37
- 239000000203 mixture Chemical class 0.000 claims description 27
- 239000000314 lubricant Substances 0.000 claims description 14
- 239000003963 antioxidant agent Substances 0.000 claims description 9
- 235000006708 antioxidants Nutrition 0.000 claims description 9
- 230000003078 antioxidant effect Effects 0.000 claims description 8
- PAYRUJLWNCNPSJ-UHFFFAOYSA-N Aniline Chemical compound NC1=CC=CC=C1 PAYRUJLWNCNPSJ-UHFFFAOYSA-N 0.000 claims description 6
- 150000002790 naphthalenes Chemical class 0.000 claims description 3
- 150000001454 anthracenes Chemical class 0.000 claims description 2
- 150000001555 benzenes Chemical class 0.000 claims description 2
- 235000010290 biphenyl Nutrition 0.000 claims description 2
- 150000004074 biphenyls Chemical class 0.000 claims description 2
- 150000002987 phenanthrenes Chemical class 0.000 claims description 2
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N phenol group Chemical group C1(=CC=CC=C1)O ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 claims description 2
- 125000003118 aryl group Chemical group 0.000 claims 2
- 239000010705 motor oil Substances 0.000 description 11
- 229920000089 Cyclic olefin copolymer Polymers 0.000 description 6
- 229920001577 copolymer Polymers 0.000 description 5
- 230000000994 depressogenic effect Effects 0.000 description 5
- 230000001050 lubricating effect Effects 0.000 description 5
- 239000003112 inhibitor Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 229920000642 polymer Polymers 0.000 description 4
- 150000001491 aromatic compounds Chemical class 0.000 description 3
- 230000005540 biological transmission Effects 0.000 description 3
- 239000003599 detergent Substances 0.000 description 3
- 238000009472 formulation Methods 0.000 description 3
- 239000003607 modifier Substances 0.000 description 3
- 229920001195 polyisoprene Polymers 0.000 description 3
- -1 polyol ester Chemical class 0.000 description 3
- PDEDQSAFHNADLV-UHFFFAOYSA-M potassium;disodium;dinitrate;nitrite Chemical compound [Na+].[Na+].[K+].[O-]N=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O PDEDQSAFHNADLV-UHFFFAOYSA-M 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 2
- RRHGJUQNOFWUDK-UHFFFAOYSA-N Isoprene Chemical compound CC(=C)C=C RRHGJUQNOFWUDK-UHFFFAOYSA-N 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 150000001993 dienes Chemical class 0.000 description 2
- 239000002270 dispersing agent Substances 0.000 description 2
- 229910001651 emery Inorganic materials 0.000 description 2
- 238000010348 incorporation Methods 0.000 description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 239000011707 mineral Substances 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- NGHTXZCKLWZPGK-UHFFFAOYSA-N nefiracetam Chemical compound CC1=CC=CC(C)=C1NC(=O)CN1C(=O)CCC1 NGHTXZCKLWZPGK-UHFFFAOYSA-N 0.000 description 2
- 239000012188 paraffin wax Substances 0.000 description 2
- 229920000193 polymethacrylate Polymers 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- SXYOAESUCSYJNZ-UHFFFAOYSA-L zinc;bis(6-methylheptoxy)-sulfanylidene-sulfido-$l^{5}-phosphane Chemical compound [Zn+2].CC(C)CCCCCOP([S-])(=S)OCCCCCC(C)C.CC(C)CCCCCOP([S-])(=S)OCCCCCC(C)C SXYOAESUCSYJNZ-UHFFFAOYSA-L 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 239000005069 Extreme pressure additive Substances 0.000 description 1
- 229920002367 Polyisobutene Polymers 0.000 description 1
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Natural products C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 1
- 240000007591 Tilia tomentosa Species 0.000 description 1
- JAWMENYCRQKKJY-UHFFFAOYSA-N [3-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-ylmethyl)-1-oxa-2,8-diazaspiro[4.5]dec-2-en-8-yl]-[2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidin-5-yl]methanone Chemical group N1N=NC=2CN(CCC=21)CC1=NOC2(C1)CCN(CC2)C(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F JAWMENYCRQKKJY-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000007866 anti-wear additive Substances 0.000 description 1
- 239000002518 antifoaming agent Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229920001400 block copolymer Polymers 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 239000003085 diluting agent Substances 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 239000010720 hydraulic oil Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 229920013639 polyalphaolefin Polymers 0.000 description 1
- 229920005862 polyol Polymers 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 150000003440 styrenes Chemical class 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M169/00—Lubricating compositions characterised by containing as components a mixture of at least two types of ingredient selected from base-materials, thickeners or additives, covered by the preceding groups, each of these compounds being essential
- C10M169/04—Mixtures of base-materials and additives
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M171/00—Lubricating compositions characterised by purely physical criteria, e.g. containing as base-material, thickener or additive, ingredients which are characterised exclusively by their numerically specified physical properties, i.e. containing ingredients which are physically well-defined but for which the chemical nature is either unspecified or only very vaguely indicated
- C10M171/02—Specified values of viscosity or viscosity index
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2205/00—Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions
- C10M2205/17—Fisher Tropsch reaction products
- C10M2205/173—Fisher Tropsch reaction products used as base material
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2020/00—Specified physical or chemical properties or characteristics, i.e. function, of component of lubricating compositions
- C10N2020/01—Physico-chemical properties
- C10N2020/02—Viscosity; Viscosity index
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2020/00—Specified physical or chemical properties or characteristics, i.e. function, of component of lubricating compositions
- C10N2020/01—Physico-chemical properties
- C10N2020/065—Saturated Compounds
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
- C10N2030/02—Pour-point; Viscosity index
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2040/00—Specified use or application for which the lubricating composition is intended
- C10N2040/04—Oil-bath; Gear-boxes; Automatic transmissions; Traction drives
- C10N2040/042—Oil-bath; Gear-boxes; Automatic transmissions; Traction drives for automatic transmissions
Definitions
- the present invention relates to an additive
- Lubricant compositions in particular for automotive crankcase or transmissions, are employed to reduce wear at metal-to-metal contact between moving parts, as well as to remove heat.
- the lubricant compositions require the presence of polymeric viscosity modifier additives to obtain the desired viscometric properties over a broad range of shear and/or
- additives are usually highly viscous liquids or solids at room temperature. In order to be able to achieve homogenous distribution, avoid handling of solids and to be able to administer the amounts of additives added into lubricant compositions and thus ensure consistent product quality, these additives are usually added as an additive concentrate.
- Example 6 of US 2005/0133407 discloses a OW-20 engine oil (i.e. a fully formulated lubricating composition, not an additive concentrate) containing 86.30 wt . % of a Fischer-Tropsch derived base oil, 0.3 wt . % of a pour point depressant and 13.4 wt . % of a PCMO DI additive package.
- OW-20 engine oil i.e. a fully formulated lubricating composition, not an additive concentrate
- the OW-20 formulation of Example 6 does not contain a viscosity index improver.
- Example 3 of WO 02/064710 discloses a 0W30 engine oil (i.e. a fully formulated lubricating composition, not an additive concentrate), containing 76.4 wt . % of a Fischer- Tropsch derived product, 14.6 wt . % of a detergent inhibitor additive package, 0.25 wt . % of a corrosion inhibitor and 10.56 wt . % of a viscosity modifier.
- Example 2 of EP 1 688 476 Al discloses a lubricating composition (i.e. not an additive concentrate) containing 18 wt . % of an additive package (see Example 1 of EP 1 688
- Emery 2925 has an aniline point (according to ASTM D 611) of 0°C and is therefore seen as a solvency booster as meant according to the present invention.
- Example 7 of US 2009/0088352 discloses a lubricating composition (i.e. not an additive concentrate) prepared to meet the John Deere J20D specification, containing 86.81 wt . % Fischer-Tropsch derived base oil, 8.10 wt . % of an additive package, 4.94 wt . % of a viscosity modifier, 0.15 wt . % of a pour point depressant and 0.07 wt . % of a foam inhibitor.
- a lubricating composition i.e. not an additive concentrate prepared to meet the John Deere J20D specification, containing 86.81 wt . % Fischer-Tropsch derived base oil, 8.10 wt . % of an additive package, 4.94 wt . % of a viscosity modifier, 0.15 wt . % of a pour point depressant and 0.07 wt . % of a foam inhibitor.
- Fischer-Tropsch derived base oils are usually not suitable as base oils to prepare additive concentrates for additives such as polymeric viscosity modifiers due to the low solvency of these Fischer-Tropsch derived base oils. Therefore,
- WO 2009/074572 suggests to include an alkylated aromatic compound (e.g. "KR 008", commercially available from King Industries) as a solvency booster in the additive concentrate.
- the solvency booster is preferably present in an amount of from
- lubricants such as hydraulic oils
- an additive concentrate comprising:
- Fischer-Tropsch derived base oils are known in the art.
- Fischer-Tropsch derived means that a material is, or derives from, a synthesis product of a Fischer-Tropsch condensation process.
- non-Fischer-Tropsch derived may be interpreted accordingly.
- a Fischer-Tropsch derived base oil will therefore be a hydrocarbon stream of which a substantial portion, except for added hydrogen, is derived directly or indirectly from a Fischer-Tropsch condensation process.
- a Fischer-Tropsch derived base oil may also be referred to as a GTL ( Gas-To-Liquids ) base oil.
- GTL Gas-To-Liquids
- base oil may refer to a mixture
- the aromatics content of a Fischer-Tropsch derived base oil will typically be below 1 wt.%, preferably below 0.5 wt . % and more preferably below 0.1 wt.%.
- the base oil has a total paraffin content of at least 80 wt.%, preferably at least 85, more preferably at least 90, yet more preferably at least 95 and most preferably at least 99 wt.%. It suitably has a saturates content (as measured by IP-368) of greater than 98 wt.%.
- the saturates content of the base oil is greater than
- the base oil preferably also has a content of naphthenic compounds of from 0 to less than 20 wt.%, more preferably of from 0.5 to 10 wt.%.
- the Fischer-Tropsch derived base oil has a kinematic viscosity at 100°C (as measured by ASTM D 7042) of from 1 to 25 mm ⁇ /s (cSt), preferably above 2.5 more preferably above 3.0 mm ⁇ /s.
- the Fischer- Tropsch derived base oil has a kinematic viscosity at 100°C of below 5.0 mm 2 /s, preferably below 4.5 mm 2 /s, more preferably below 4.2 mm 2 /s.
- the Fischer-Tropsch derived base oil typically has a kinematic viscosity at 40°C (as measured by ASTM D 7042) of from 10 to 100 mm 2 /s (cSt), preferably from 15 to 50 mm ⁇ /s.
- the Fischer-Tropsch derived base oil preferably has a pour point (as measured according to ASTM D 5950) of below -30°C, more preferably below -40°C, and most preferably below -45°C.
- the flash point (as measured by ASTM D92) of the Fischer-Tropsch derived base oil is preferably greater than 120°C, more preferably even greater than 140 °C.
- the Fischer-Tropsch derived base oil preferably has a viscosity index (according to ASTM D 2270) in the range of from 100 to 200.
- the Fischer-Tropsch derived base oil has a viscosity index of at least 125, preferably 130. Also it is preferred that the viscosity index is below 180, preferably below 150.
- Fischer-Tropsch derived base oil contains a blend of two or more Fischer-Tropsch derived base oils
- the above values apply to the blend of the two or more Fischer-Tropsch derived base oils.
- the additive concentrate may comprise one or more non-reacted Fischer-Tropsch derived base oil
- Fischer-Tropsch derived base oils such as mineral derived base oils and so-called synthetic base oils (such as PAOs) including Group I-V base oils according to the definitions of American Petroleum Institute (API).
- API American Petroleum Institute
- the additive concentrate according to the present invention comprises at least 80 wt . % of the Fischer-Tropsch derived base oil, preferably at least 90 wt.%, based on the total weight of the additive concentrate. Also it is preferred that the additive concentrate comprises less than 10.0 wt.% of a non-FT- derived base oil, preferably less than 5.0 wt.%, more preferably less than 2.0 wt.%, even more preferably less than 1.0 wt.%, based on the total weight of the additive concentrate. Most preferably the additive concentrate comprises no non-Fischer-Tropsch derived base oils at all . There are no particular limitations regarding the viscosity modifier as used in the additive concentrate according to the present invention. As a person skilled in the art is familiar with the term "viscosity modifier as used in the additive concentrate according to the present invention. As a person skilled in the art is familiar with the term "viscosity modifier as used in the additive concentrate according to the present invention. As a person skilled in the art is familiar with the
- Viscosity modifiers also known as VI improvers
- viscosity index improvers or viscosity improvers provide lubricants with high- and low-temperature operability; these additives impart acceptable viscosity at low temperatures and are preferably shear stable.
- a viscosity modifier improves (e.g. by at least 5 units) the viscosity index (e.g. as determined by ASTM D 2270) by its incorporation in the additive concentrate (and/or a fully formulated lubricant composition in which the viscosity modifier is incorporated) .
- the additive concentrate comprises at least 3.0 wt . % of a viscosity modifier, based on the total weight of the additive concentrate.
- the additive concentrate comprises at least 5.0 wt . % such as from 5.0 to 10.0 wt.%, preferably from 6.0 to 10.0 wt . % of the viscosity modifier, based on the total weight of the additive concentrate .
- Non-limiting examples of viscosity modifiers are linear or star-shaped olefin copolymers,
- polyisobutylenes polymethacrylates , polymers of a diene such as isoprene or butadiene, or a copolymer of such a diene with optionally substituted styrene.
- copolymers are preferably hydrogenated to such an extent as to saturate most of the olefinic unsaturation .
- a number of other types of viscosity modifier are known in the art, and many of these are described in Proceedings of Conference "Viscosity and flow properties of
- dispersancy e.g. dispersant viscosity index improvers based on block copolymers, or polymethacrylates
- antioxidant functionality as well as viscosity
- depressants mixed in to give handleable products in cold climates .
- the viscosity modifier is selected from the group consisting of olefin copolymers, polyisoprene polymers and diene-styrene copolymers.
- Olefin copolymers are commercially available from Chevron Oronite Company LLC under the trade designation "PARATONE®" (such as
- HiTEC® such as “HiTEC® 5850B”; and from The Lubrizol
- Polyisoprene polymers are commercially available from Infineum International Limited, e.g. under the trade designation "SV200"; diene-styrene copolymers are commercially available from Infineum International
- the additive concentrate according to the present invention comprises less than 5.0 wt . % of a solvency booster, based on the total weight of the additive concentrate.
- the additive concentrate comprises less than 2.0 wt.%, preferably less than 1.0 wt.%, more preferably less than 0.5 wt.%, of the solvency booster, based on the total weight of the additive concentrate. It is even more preferred that the additive concentrate contains no solvency booster at all.
- the solvency booster is a compound having an aniline point (according to ASTM D 611) of less than 100°C.
- the solvency booster is an alkylated aromatic compound.
- Alkylated aromatic compounds include alkylated benzenes, alkylated anthracenes, alkylated phenanthrenes , alkylated biphenyls, and alkylated naphthalenes or any mixtures thereof.
- alkylated naphthalenes reference is made to WO 2009/074572.
- the additive concentrate may further contain a pour point depressant to improve pumpability.
- the pour point depressant preferably is present in a range of from 0.5 to 3 wt.%, more preferably from 1 to 2 wt.%, and most preferably from 1.1. to 1.4 wt.%.
- the additive concentrate preferably has - when normalized at a concentration of viscosity modifier of 1.0 wt.% - a dynamic viscosity at -30°C (according to ASTM D 5293) of below 3000 cP and a kinematic viscosity at 100°C (according to ASTM D 7042) of at least 5.5 cSt .
- the dynamic viscosity at -30°C is below
- concentrates containing different amounts of viscosity modifier can be normalized to a concentration of 1.0 wt.% by diluting the concentrate with the appropriate amount of the same base oil (or base oil blend) used to make the additive concentrate. Further it is preferred that the additive concentrate comprises from 5 to 500 ppm of an anti-oxidant,
- a phenolic and an aminic antioxidant preferably selected from a phenolic and an aminic antioxidant, or a mixture thereof.
- the present invention provides a lubricant composition
- a lubricant composition comprising a base oil, one or more additives other than a viscosity modifier and the additive concentrate according to the present invention.
- This base oil may be a Fischer- Tropsch derived base oil, a non-Fischer-Tropsch derived base oil or a mixture thereof.
- the one or more additives other than a viscosity modifier may be selected from a broad range of additives such as anti-oxidants , anti-wear additives, dispersants, detergents, over-based detergents, extreme pressure additives, friction modifiers, pour point depressants, metal passivators, corrosion inhibitors, demulsifiers , anti-foam agents, seal compatibility agents and additive diluent base oils, etc.
- additives such as anti-oxidants , anti-wear additives, dispersants, detergents, over-based detergents, extreme pressure additives, friction modifiers, pour point depressants, metal passivators, corrosion inhibitors, demulsifiers , anti-foam agents, seal compatibility agents and additive diluent base oils, etc.
- additives such as anti-oxidants , anti-wear additives, dispersants, detergents, over-based detergents, extreme pressure additives, friction modifiers, pour point depressants, metal passivators, corrosion inhibitors, demulsifiers ,
- Table 1 indicates the properties for the base oils used in the additive concentrates.
- Tables 2-5 indicate the composition and properties of the formulated additive concentrates that were tested; the amounts of the components are given in wt.%, based on the total weight of the additive concentrate.
- Table 6 exemplifies the storage stability properties of an additive concentrate according to the present invention.
- Table 7 exemplifies a fully formulated lubricating compositions (i.e. a SAE 5W-30 engine oil), comprising the additive concentrate according to the present invention.
- the viscosities and Viscosity Index as measured for the additive concentrates were all measured at a normalized Viscosity Modifier concentration of 1.0 wt.% by dilution with the same base oil used to blend the additive concentrate (as the neat concentrates were too thick and therefore outside the testing range of the indicated test methods) .
- All tested additive concentrates contained a combination of a base oil and a viscosity modifier, and optionally an anti-oxidant .
- Base oil 1 was a Fischer-Tropsch derived base oil (“GTL 4") having a kinematic viscosity at 100°C (ASTM D 7042) of approx. 4 cSt (mm 2 /s) .
- This GTL 4 base oil may be conveniently manufactured by the process described in e.g. WO-A-02/070631, the teaching of which is hereby incorporated by reference.
- Base oil 2 was a commercially available Group I base oil having a kinematic viscosity at 100°C (ASTM D 7042) of approx. 4 cSt .
- Base oil 2 is commercially available from ExxonMobil Corporation under the trade designation "Americas SN 115".
- Base oil 3 was a commercially available Group II base oil having a kinematic viscosity at 100°C (ASTM D 7042) of approx. 4.7 cSt .
- Base oil 3 is commercially available from Motiva Enterprises LLC under the trade designation "Star 5+”.
- Base oil 4" was a commercially available Group II base oil having a kinematic viscosity at 100°C (ASTM D
- Base oil 4 is commercially available from Motiva Enterprises LLC under the trade designation "Star 6".
- VMV was a commercially available olefin copolymer viscosity modifier available from Chevron Oronite Company
- VM2 was a commercially available olefin copolymer viscosity modifier available from Afton Chemical
- VM3 was a commercially available olefin copolymer viscosity modifier available from The Lubrizol
- VM4 was a commercially available polyisoprene polymer viscosity modifier available from Infineum
- VM5 was a commercially available diene-styrene copolymer viscosity modifier available from Infineum International Limited under the trade designation "SV 260”.
- Anti-oxidant was a commercially available aminic anti-oxidant available from Ciba Corporation (Houston,
- Example 1-8 and Comparative Examples 1-8 were obtained by mixing the base oils with the viscosity modifier using a Silverson high shear mixer and following (conventional) blending procedures
- the additive package contained a pour point depressant and other typical additives for use in a SAE 5W-30 engine oil.
- the present invention now surprisingly provides the possibility to prepare additive concentrates containing a viscosity modifier using Fischer-Tropsch derived base oils, but without significant amounts of solvency boosters or even without the use of solvency boosters at all. Also, it can be seen that the additive concentrates according to the present invention show, when compared with conventional additive concentrates using mineral derived Group I (i.e. non-Fischer-Tropsch derived) base oils, significantly better low temperature properties, which is highly desirable for formulating multi-grade lubricants.
- mineral derived Group I i.e. non-Fischer-Tropsch derived
- the additive concentrates according to the present invention have excellent storage stability at various temperatures for extended periods of time.
- the additive concentrates according to the present invention are suitable for use in a wide range of lubricants, such as in e.g. engine oils and transmission fluids and other lubricants for which a viscosity modifier is desired.
- lubricants such as in e.g. engine oils and transmission fluids and other lubricants for which a viscosity modifier is desired.
- SAE 5W-30 formulations can be formulated when using the additive concentrates according to the present invention.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Lubricants (AREA)
Abstract
The present invention provides an additive concentrate comprising: - at least 90 wt. % of a Fischer-Tropsch derived base oil, based on the total weight of the additive concentrate; - at least 3.0 wt. % of a viscosity modifier, based on the total weight of the additive concentrate; and - less than 5.0 wt. % of a solvency booster, based on the total weight of the additive concentrate.
Description
ADDITIVE CONCENTRATE
The present invention relates to an additive
concentrate comprising a base oil and a viscosity modifier, for the incorporation into a lubricant
composition .
Lubricant compositions, in particular for automotive crankcase or transmissions, are employed to reduce wear at metal-to-metal contact between moving parts, as well as to remove heat. In many applications, the lubricant compositions require the presence of polymeric viscosity modifier additives to obtain the desired viscometric properties over a broad range of shear and/or
temperatures. These additives are usually highly viscous liquids or solids at room temperature. In order to be able to achieve homogenous distribution, avoid handling of solids and to be able to administer the amounts of additives added into lubricant compositions and thus ensure consistent product quality, these additives are usually added as an additive concentrate.
Example 6 of US 2005/0133407 discloses a OW-20 engine oil (i.e. a fully formulated lubricating composition, not an additive concentrate) containing 86.30 wt . % of a Fischer-Tropsch derived base oil, 0.3 wt . % of a pour point depressant and 13.4 wt . % of a PCMO DI additive package. As is clear from paragraph [0147] of US
2005/0133407, the OW-20 formulation of Example 6 does not contain a viscosity index improver.
Example 3 of WO 02/064710 discloses a 0W30 engine oil (i.e. a fully formulated lubricating composition, not an additive concentrate), containing 76.4 wt . % of a Fischer- Tropsch derived product, 14.6 wt . % of a detergent
inhibitor additive package, 0.25 wt . % of a corrosion inhibitor and 10.56 wt . % of a viscosity modifier.
Example 2 of EP 1 688 476 Al discloses a lubricating composition (i.e. not an additive concentrate) containing 18 wt . % of an additive package (see Example 1 of EP 1 688
476 Al) blended with (90% x 82 wt . % =) 73.8 wt . % of a Fischer-Tropsch derived base oil and (10% x 82 wt . % =) 8.2 wt . % of Emery 2925 (a triesterified polyol ester derived from C8-Ci0 acids) available from Cognis
Corporation. As can be learned from Table II of US
2007/0093396, Emery 2925 has an aniline point (according to ASTM D 611) of 0°C and is therefore seen as a solvency booster as meant according to the present invention.
Example 7 of US 2009/0088352 discloses a lubricating composition (i.e. not an additive concentrate) prepared to meet the John Deere J20D specification, containing 86.81 wt . % Fischer-Tropsch derived base oil, 8.10 wt . % of an additive package, 4.94 wt . % of a viscosity modifier, 0.15 wt . % of a pour point depressant and 0.07 wt . % of a foam inhibitor.
As acknowledged in WO 2009/074572, Fischer-Tropsch derived base oils are usually not suitable as base oils to prepare additive concentrates for additives such as polymeric viscosity modifiers due to the low solvency of these Fischer-Tropsch derived base oils. Therefore,
WO 2009/074572 suggests to include an alkylated aromatic compound (e.g. "KR 008", commercially available from King Industries) as a solvency booster in the additive concentrate. According to WO 2009/074572, the solvency booster is preferably present in an amount of from
25 wt . % to 75 wt.%, based on the weight of the additive concentrate .
The present applicant has now surprisingly found that it is possible to prepare additive concentrates
containing a viscosity modifier using Fischer-Tropsch derived base oils, which additive concentrates are suitable for use in e.g. transmission oils and engine oils and other lubricants (including industrial
lubricants such as hydraulic oils) for which a viscosity modifier is desired, but without the need of significant amounts of solvency boosters, or even without the need of solvency boosters at all.
To this end the present invention provides an additive concentrate comprising:
- at least 90 wt . % of a Fischer-Tropsch derived base oil, based on the total weight of the additive concentrate; - at least 3.0 wt . % of a viscosity modifier, based on the total weight of the additive concentrate; and
- less than 5.0 wt . % of a solvency booster, based on the total weight of the additive concentrate.
Fischer-Tropsch derived base oils are known in the art. In the present context, the term "Fischer-Tropsch derived" means that a material is, or derives from, a synthesis product of a Fischer-Tropsch condensation process. The term "non-Fischer-Tropsch derived" may be interpreted accordingly. A Fischer-Tropsch derived base oil will therefore be a hydrocarbon stream of which a substantial portion, except for added hydrogen, is derived directly or indirectly from a Fischer-Tropsch condensation process. A Fischer-Tropsch derived base oil may also be referred to as a GTL ( Gas-To-Liquids ) base oil. The term "base oil" may refer to a mixture
containing more than one base oil.
For further information on the Fischer-Tropsch derived base oil and the preparation thereof reference is
made to the above-mentioned WO 2009/074572, the teaching of which is hereby incorporated by specific reference.
Typically, the aromatics content of a Fischer-Tropsch derived base oil, suitably determined by ASTM D 4629, will typically be below 1 wt.%, preferably below 0.5 wt . % and more preferably below 0.1 wt.%. Suitably, the base oil has a total paraffin content of at least 80 wt.%, preferably at least 85, more preferably at least 90, yet more preferably at least 95 and most preferably at least 99 wt.%. It suitably has a saturates content (as measured by IP-368) of greater than 98 wt.%. Preferably the saturates content of the base oil is greater than
99 wt.%, more preferably greater than 99.5 wt.%. It further preferably has a maximum n-paraffin content of 0.5 wt . % . The base oil preferably also has a content of naphthenic compounds of from 0 to less than 20 wt.%, more preferably of from 0.5 to 10 wt.%.
Typically, the Fischer-Tropsch derived base oil has a kinematic viscosity at 100°C (as measured by ASTM D 7042) of from 1 to 25 mm^/s (cSt), preferably above 2.5 more preferably above 3.0 mm^/s. Preferably, the Fischer- Tropsch derived base oil has a kinematic viscosity at 100°C of below 5.0 mm2/s, preferably below 4.5 mm2/s, more preferably below 4.2 mm2/s.
Further, the Fischer-Tropsch derived base oil typically has a kinematic viscosity at 40°C (as measured by ASTM D 7042) of from 10 to 100 mm2/s (cSt), preferably from 15 to 50 mm^/s.
Also, the Fischer-Tropsch derived base oil preferably has a pour point (as measured according to ASTM D 5950) of below -30°C, more preferably below -40°C, and most preferably below -45°C.
The flash point (as measured by ASTM D92) of the Fischer-Tropsch derived base oil is preferably greater than 120°C, more preferably even greater than 140 °C.
The Fischer-Tropsch derived base oil preferably has a viscosity index (according to ASTM D 2270) in the range of from 100 to 200. Preferably, the Fischer-Tropsch derived base oil has a viscosity index of at least 125, preferably 130. Also it is preferred that the viscosity index is below 180, preferably below 150.
In the event the Fischer-Tropsch derived base oil contains a blend of two or more Fischer-Tropsch derived base oils, the above values apply to the blend of the two or more Fischer-Tropsch derived base oils.
In addition to the Fischer-Tropsch derived base oil, the additive concentrate may comprise one or more non-
Fischer-Tropsch derived base oils, such as mineral derived base oils and so-called synthetic base oils (such as PAOs) including Group I-V base oils according to the definitions of American Petroleum Institute (API). These API categories are defined in API Publication 1509, 15th
Edition, Appendix E, July 2009.
Preferably the additive concentrate according to the present invention comprises at least 80 wt . % of the Fischer-Tropsch derived base oil, preferably at least 90 wt.%, based on the total weight of the additive concentrate. Also it is preferred that the additive concentrate comprises less than 10.0 wt.% of a non-FT- derived base oil, preferably less than 5.0 wt.%, more preferably less than 2.0 wt.%, even more preferably less than 1.0 wt.%, based on the total weight of the additive concentrate. Most preferably the additive concentrate comprises no non-Fischer-Tropsch derived base oils at all .
There are no particular limitations regarding the viscosity modifier as used in the additive concentrate according to the present invention. As a person skilled in the art is familiar with the term "viscosity
modifier", this is not further discussed in detail.
Viscosity modifiers (also known as VI improvers,
viscosity index improvers or viscosity improvers) provide lubricants with high- and low-temperature operability; these additives impart acceptable viscosity at low temperatures and are preferably shear stable. Typically, and as meant according to the present invention, a viscosity modifier improves (e.g. by at least 5 units) the viscosity index (e.g. as determined by ASTM D 2270) by its incorporation in the additive concentrate (and/or a fully formulated lubricant composition in which the viscosity modifier is incorporated) .
According to the present invention, the additive concentrate comprises at least 3.0 wt . % of a viscosity modifier, based on the total weight of the additive concentrate. Preferably, the additive concentrate comprises at least 5.0 wt . % such as from 5.0 to 10.0 wt.%, preferably from 6.0 to 10.0 wt . % of the viscosity modifier, based on the total weight of the additive concentrate .
Non-limiting Examples of viscosity modifiers are linear or star-shaped olefin copolymers,
polyisobutylenes , polymethacrylates , polymers of a diene such as isoprene or butadiene, or a copolymer of such a diene with optionally substituted styrene. These
copolymers are preferably hydrogenated to such an extent as to saturate most of the olefinic unsaturation . A number of other types of viscosity modifier are known in the art, and many of these are described in Proceedings
of Conference "Viscosity and flow properties of
multigrade engine oils", Esslingen, Germany, December 1977. It is also known in the art that viscosity
modifiers can be functionalised to incorporate
dispersancy (e.g. dispersant viscosity index improvers based on block copolymers, or polymethacrylates ) and/or antioxidant functionality as well as viscosity
modification and they can also have pour point
depressants mixed in to give handleable products in cold climates .
Preferably, the viscosity modifier is selected from the group consisting of olefin copolymers, polyisoprene polymers and diene-styrene copolymers. Olefin copolymers are commercially available from Chevron Oronite Company LLC under the trade designation "PARATONE®" (such as
"PARATONE® 8921" and "PARATONE® 8941") ; from Afton
Chemical Corporation under the trade designation "HiTEC®" (such as "HiTEC® 5850B"; and from The Lubrizol
Corporation under the trade designation "Lubrizol®
7067C". Polyisoprene polymers are commercially available from Infineum International Limited, e.g. under the trade designation "SV200"; diene-styrene copolymers are commercially available from Infineum International
Limited, e.g. under the trade designation "SV 260".
The additive concentrate according to the present invention comprises less than 5.0 wt . % of a solvency booster, based on the total weight of the additive concentrate. Preferably, the additive concentrate comprises less than 2.0 wt.%, preferably less than 1.0 wt.%, more preferably less than 0.5 wt.%, of the solvency booster, based on the total weight of the additive concentrate. It is even more preferred that the additive concentrate contains no solvency booster at all.
There are no particular limitations regarding the solvency booster as meant according to the present invention. As a person skilled in the art is familiar with the term "solvency booster", this is not further discussed in detail. Typically, and as meant according to the present invention, a solvency booster is a compound having an aniline point (according to ASTM D 611) of less than 100°C.
Preferably, the solvency booster is an alkylated aromatic compound. Alkylated aromatic compounds include alkylated benzenes, alkylated anthracenes, alkylated phenanthrenes , alkylated biphenyls, and alkylated naphthalenes or any mixtures thereof. For further description of the alkylated naphthalenes, reference is made to WO 2009/074572.
The additive concentrate may further contain a pour point depressant to improve pumpability. If present, the pour point depressant preferably is present in a range of from 0.5 to 3 wt.%, more preferably from 1 to 2 wt.%, and most preferably from 1.1. to 1.4 wt.%.
The additive concentrate preferably has - when normalized at a concentration of viscosity modifier of 1.0 wt.% - a dynamic viscosity at -30°C (according to ASTM D 5293) of below 3000 cP and a kinematic viscosity at 100°C (according to ASTM D 7042) of at least 5.5 cSt .
Preferably the dynamic viscosity at -30°C is below
2000 cP, more preferably below 1500 cP . Additive
concentrates containing different amounts of viscosity modifier can be normalized to a concentration of 1.0 wt.% by diluting the concentrate with the appropriate amount of the same base oil (or base oil blend) used to make the additive concentrate.
Further it is preferred that the additive concentrate comprises from 5 to 500 ppm of an anti-oxidant,
preferably selected from a phenolic and an aminic antioxidant, or a mixture thereof.
In a further aspect the present invention provides a lubricant composition comprising a base oil, one or more additives other than a viscosity modifier and the additive concentrate according to the present invention.
There are no particular limitations regarding the base oil as used in the lubricant composition according to the present invention. This base oil may be a Fischer- Tropsch derived base oil, a non-Fischer-Tropsch derived base oil or a mixture thereof.
The one or more additives other than a viscosity modifier may be selected from a broad range of additives such as anti-oxidants , anti-wear additives, dispersants, detergents, over-based detergents, extreme pressure additives, friction modifiers, pour point depressants, metal passivators, corrosion inhibitors, demulsifiers , anti-foam agents, seal compatibility agents and additive diluent base oils, etc. As the person skilled in the art is familiar with the above and other additives, these are not further discussed here in detail. Specific examples of such additives are described in for example Kirk- Othmer Encyclopedia of Chemical Technology, third edition, volume 14, pages 477-526.
The present invention is described below with
reference to the following Examples, which are not intended to limit the scope of the present invention in any way .
EXAMPLES
Additive Concentrates
Various additive concentrates were formulated.
Table 1 indicates the properties for the base oils used
in the additive concentrates. Tables 2-5 indicate the composition and properties of the formulated additive concentrates that were tested; the amounts of the components are given in wt.%, based on the total weight of the additive concentrate. Table 6 exemplifies the storage stability properties of an additive concentrate according to the present invention. Further, Table 7 exemplifies a fully formulated lubricating compositions (i.e. a SAE 5W-30 engine oil), comprising the additive concentrate according to the present invention.
The viscosities and Viscosity Index as measured for the additive concentrates were all measured at a normalized Viscosity Modifier concentration of 1.0 wt.% by dilution with the same base oil used to blend the additive concentrate (as the neat concentrates were too thick and therefore outside the testing range of the indicated test methods) .
All tested additive concentrates contained a combination of a base oil and a viscosity modifier, and optionally an anti-oxidant .
"Base oil 1" was a Fischer-Tropsch derived base oil ("GTL 4") having a kinematic viscosity at 100°C (ASTM D 7042) of approx. 4 cSt (mm2/s) . This GTL 4 base oil may be conveniently manufactured by the process described in e.g. WO-A-02/070631, the teaching of which is hereby incorporated by reference.
"Base oil 2 " was a commercially available Group I base oil having a kinematic viscosity at 100°C (ASTM D 7042) of approx. 4 cSt . Base oil 2 is commercially available from ExxonMobil Corporation under the trade designation "Americas SN 115".
"Base oil 3" was a commercially available Group II base oil having a kinematic viscosity at 100°C (ASTM D
7042) of approx. 4.7 cSt . Base oil 3 is commercially available from Motiva Enterprises LLC under the trade designation "Star 5+".
"Base oil 4" was a commercially available Group II base oil having a kinematic viscosity at 100°C (ASTM D
7042) of approx. 6.5 cSt. Base oil 4 is commercially available from Motiva Enterprises LLC under the trade designation "Star 6".
"VMl" was a commercially available olefin copolymer viscosity modifier available from Chevron Oronite Company
LLC (Richmond, California, USA) under the trade
designation "PARATONE® 8921".
"VM2" was a commercially available olefin copolymer viscosity modifier available from Afton Chemical
Corporation (Richmond, Virginia, USA) under the trade designation "HiTEC® 5850B".
"VM3" was a commercially available olefin copolymer viscosity modifier available from The Lubrizol
Corporation (Wickliffe, Ohio, USA) under the trade designation "Lubrizol® 7067C".
"VM4" was a commercially available polyisoprene polymer viscosity modifier available from Infineum
International Limited (Linden, New Jersey, USA) under the trade designation "SV 200".
"VM5" was a commercially available diene-styrene copolymer viscosity modifier available from Infineum International Limited under the trade designation "SV 260".
"Anti-oxidant" was a commercially available aminic anti-oxidant available from Ciba Corporation (Houston,
Texas, USA) under the trade designation " Ciba® IRGANOX® L57" .
The compositions of Example 1-8 and Comparative Examples 1-8 were obtained by mixing the base oils with the viscosity modifier using a Silverson high shear mixer and following (conventional) blending procedures
recommended by the suppliers of the Viscosity Modifiers.
TABLE 1
According to ASTM D 5293
2According to ASTM D 7042
3According to ASTM D 2270
According to ASTM D 611
5According to ASTM D 5950
6According to ASTM D 5800B
7According to IP 368 (modified)
TABLE 2 - Additive concentrates containing VMl
According to ASTM D 5293. NB 1 cP (centi Poise) = 1 mPa . s
According to ASTM D 7042
3According to ASTM D 2270
TABLE 3 - Additive concentrates containing VM2
According to ASTM D 5293
According to ASTM D 7042
3According to ASTM D 2270
TABLE 4 - Additive concentrates containing VM3
According to ASTM D 5293
According to ASTM D 7042
3According to ASTM D 2270
*Not according to the present invention
TABLE 5 - Additive concentrates containing VM4 or VM5
According to ASTM D 5293
According to ASTM D 7042
3According to ASTM D 2270
*Not according to the present invention
Storage Stability
In order to demonstrate the storage stability properties of the additive concentrates according to the present invention, separate samples of the additive concentrate of Example 1 were stored for 30 days at temperatures of 70°C, ambient (20°C), 0°C and -20°C, respectively. The measured viscosities after 30 days of storage are indicated in Table 6 below. Similar good stability properties were obtained for the additive concentrates of Examples 2-8.
TABLE 6 - Storage stability of additive concentrate of Example 1
According to ASTM D 5293
According to ASTM D 7042
According to ASTM D 2270
SAE 5W30 engine oils
Whilst using the additive concentrates of Example 2 and 4 above and a conventional additive package, two SAE 5W-30 engine oil formulations (Examples 9 and 10) were prepared meeting the so-called SAE J300 Specifications
(as revised in January 2009) . SAE stands for Society of Automotive Engineers.
The amounts of the components and the properties of the 5W-30 engine oil are indicated in Table 7 below.
The additive package contained a pour point depressant and other typical additives for use in a SAE 5W-30 engine oil.
TABLE 7 - SAE 5W-30 engine oils
According to ASTM D 5293
According to ASTM D 7042
3According to ASTM D 2270
According to ASTM D 4684
According to ASTM D 4683
Discussion
As can be learned from Tables 2-5, the present invention now surprisingly provides the possibility to prepare additive concentrates containing a viscosity modifier using Fischer-Tropsch derived base oils, but without significant amounts of solvency boosters or even without the use of solvency boosters at all. Also, it can be seen that the additive concentrates according to the present invention show, when compared with conventional additive concentrates using mineral derived Group I (i.e. non-Fischer-Tropsch derived) base oils, significantly better low temperature properties, which is highly desirable for formulating multi-grade lubricants.
Furthermore, as exemplified by Table 6, the additive concentrates according to the present invention have excellent storage stability at various temperatures for extended periods of time.
The additive concentrates according to the present invention are suitable for use in a wide range of lubricants, such as in e.g. engine oils and transmission fluids and other lubricants for which a viscosity modifier is desired. As shown in Table 7, SAE 5W-30 formulations can be formulated when using the additive concentrates according to the present invention.
Claims
1. An additive concentrate comprising:
- at least 90 wt . % of a Fischer-Tropsch derived base oil, based on the total weight of the additive concentrate;
- at least 3.0 wt . % of a viscosity modifier, based on the total weight of the additive concentrate; and
- less than 5.0 wt . % of a solvency booster, based on the total weight of the additive concentrate.
2. Additive concentrate according to claim 1,
wherein the additive concentrate comprises less than 10.0 wt . % of a non-Fischer-Tropsch derived base oil, preferably less than 5.0 wt.%, more preferably less than 2.0 wt.%, even more preferably less than 1.0 wt.%, based on the total weight of the additive concentrate.
3. Additive concentrate according to claim 1 or 2, wherein the Fischer-Tropsch derived base oil has a kinematic viscosity at 100°C (according to ASTM D7042) of below 5.0 mm2/s, preferably below 4.5 mm2/s, more
preferably below 4.2 mm2/s.
4. Additive concentrate according to any one of claims 1 to 3, wherein the Fischer-Tropsch derived base oil has a
Viscosity Index (according to ASTM D 2270) of at least 125, preferably at least 130.
5. Additive concentrate according to any one of claims 1 to 4, wherein the additive concentrate comprises from 5.0 to 10 wt.% of the viscosity modifier, based on the total weight of the additive concentrate.
6. Additive concentrate according to any one of claims 1 to 5, wherein the additive concentrate comprises less than 2.0 wt.%, preferably less than 1.0 wt.%, more preferably less than 0.5 wt.%, of the solvency booster, based on the total weight of the additive concentrate.
7. Additive concentrate according to any one of claims 1 to 6, wherein the solvency booster has an aniline point (according to ASTM D 611) of less than 100°C.
8. Additive concentrate according to any one of claims 1 to 7, wherein the solvency booster is an alkylated aromatic component .
9. Additive concentrate according to claim 8, wherein the alkylated aromatic component is selected from alkylated benzenes, alkylated anthracenes, alkylated phenanthrenes , alkylated biphenyls, and alkylated naphthalenes, or any mixtures thereof.
10. Additive concentrate according to any one of claims 1 to 9, wherein the additive concentrate when normalized at a concentration of viscosity modifier of 1.0 wt.% has a dynamic viscosity at -30°C (according to ASTM D 5293) of below 3000 cP and a kinematic viscosity at 100°C
(according to ASTM D 7042) of at least 5.5 cSt .
11. Additive concentrate according to any one of claims 1 to 10, further comprising 5 to 500 ppm of an antioxidant, preferably selected from a phenolic and aminic anti-oxidant, or a mixture thereof.
12. A lubricant composition comprising a base oil, one or more additives other than a viscosity modifier and the additive concentrate according to any one of claims 1 to 11.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP10784756A EP2504416A1 (en) | 2009-11-25 | 2010-11-23 | Additive concentrate |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP09177029A EP2192168A1 (en) | 2009-11-25 | 2009-11-25 | Additive concentrate |
| EP10784756A EP2504416A1 (en) | 2009-11-25 | 2010-11-23 | Additive concentrate |
| PCT/EP2010/067995 WO2011064194A1 (en) | 2009-11-25 | 2010-11-23 | Additive concentrate |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| EP2504416A1 true EP2504416A1 (en) | 2012-10-03 |
Family
ID=42101346
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP09177029A Withdrawn EP2192168A1 (en) | 2009-11-25 | 2009-11-25 | Additive concentrate |
| EP10784756A Withdrawn EP2504416A1 (en) | 2009-11-25 | 2010-11-23 | Additive concentrate |
Family Applications Before (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP09177029A Withdrawn EP2192168A1 (en) | 2009-11-25 | 2009-11-25 | Additive concentrate |
Country Status (7)
| Country | Link |
|---|---|
| US (1) | US20120302480A1 (en) |
| EP (2) | EP2192168A1 (en) |
| JP (1) | JP2013512296A (en) |
| CN (1) | CN102686711A (en) |
| BR (1) | BR112012012373A2 (en) |
| RU (1) | RU2012126169A (en) |
| WO (1) | WO2011064194A1 (en) |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10829709B2 (en) * | 2014-01-02 | 2020-11-10 | Infineum International Limited | Viscosity index improver concentrates for lubricating oil compositions |
| CN105861131A (en) * | 2016-04-28 | 2016-08-17 | 浙江康力博能源科技有限公司 | Energy-saving vehicle gear oil and preparation method thereof |
| US20180305633A1 (en) * | 2017-04-19 | 2018-10-25 | Shell Oil Company | Lubricating compositions comprising a volatility reducing additive |
Family Cites Families (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6790386B2 (en) * | 2000-02-25 | 2004-09-14 | Petro-Canada | Dielectric fluid |
| AU2002249198B2 (en) * | 2001-02-13 | 2006-10-12 | Shell Internationale Research Maatschappij B.V. | Lubricant composition |
| AR032941A1 (en) | 2001-03-05 | 2003-12-03 | Shell Int Research | A PROCEDURE TO PREPARE A LUBRICATING BASE OIL AND BASE OIL OBTAINED, WITH ITS VARIOUS USES |
| US20030166474A1 (en) * | 2002-01-31 | 2003-09-04 | Winemiller Mark D. | Lubricating oil compositions with improved friction properties |
| US20030158055A1 (en) * | 2002-01-31 | 2003-08-21 | Deckman Douglas Edward | Lubricating oil compositions |
| US7195706B2 (en) * | 2003-12-23 | 2007-03-27 | Chevron U.S.A. Inc. | Finished lubricating comprising lubricating base oil with high monocycloparaffins and low multicycloparaffins |
| US7465696B2 (en) * | 2005-01-31 | 2008-12-16 | Chevron Oronite Company, Llc | Lubricating base oil compositions and methods for improving fuel economy in an internal combustion engine using same |
| GB2439027B (en) * | 2005-03-11 | 2009-10-28 | Chevron Usa Inc | Extra light hydrocarbon liquids |
| US7674364B2 (en) * | 2005-03-11 | 2010-03-09 | Chevron U.S.A. Inc. | Hydraulic fluid compositions and preparation thereof |
| EP1937792A1 (en) * | 2005-10-17 | 2008-07-02 | Shell Internationale Research Maatschappij B.V. | Lubricating oil composition |
| US7732386B2 (en) * | 2005-10-25 | 2010-06-08 | Chevron U.S.A. Inc. | Rust inhibitor for highly paraffinic lubricating base oil |
| US20090088352A1 (en) * | 2007-09-27 | 2009-04-02 | Chevron U.S.A. Inc. | Tractor hydraulic fluid compositions and preparation thereof |
| EP2072610A1 (en) | 2007-12-11 | 2009-06-24 | Shell Internationale Research Maatschappij B.V. | Carrier oil composition |
| CN102803446A (en) * | 2009-06-24 | 2012-11-28 | 国际壳牌研究有限公司 | Lubricating Composition |
-
2009
- 2009-11-25 EP EP09177029A patent/EP2192168A1/en not_active Withdrawn
-
2010
- 2010-11-23 EP EP10784756A patent/EP2504416A1/en not_active Withdrawn
- 2010-11-23 WO PCT/EP2010/067995 patent/WO2011064194A1/en not_active Ceased
- 2010-11-23 US US13/511,392 patent/US20120302480A1/en not_active Abandoned
- 2010-11-23 JP JP2012540400A patent/JP2013512296A/en active Pending
- 2010-11-23 RU RU2012126169/04A patent/RU2012126169A/en not_active Application Discontinuation
- 2010-11-23 BR BR112012012373A patent/BR112012012373A2/en not_active IP Right Cessation
- 2010-11-23 CN CN2010800530915A patent/CN102686711A/en active Pending
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| Title |
|---|
| See references of WO2011064194A1 * |
Also Published As
| Publication number | Publication date |
|---|---|
| BR112012012373A2 (en) | 2017-07-04 |
| JP2013512296A (en) | 2013-04-11 |
| EP2192168A1 (en) | 2010-06-02 |
| RU2012126169A (en) | 2013-12-27 |
| WO2011064194A1 (en) | 2011-06-03 |
| CN102686711A (en) | 2012-09-19 |
| US20120302480A1 (en) | 2012-11-29 |
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