WO1996017041A1 - Melanges polymeres contenant des copolymeres d'olefines et des polymeres ramifies en etoile - Google Patents
Melanges polymeres contenant des copolymeres d'olefines et des polymeres ramifies en etoile Download PDFInfo
- Publication number
- WO1996017041A1 WO1996017041A1 PCT/US1995/015707 US9515707W WO9617041A1 WO 1996017041 A1 WO1996017041 A1 WO 1996017041A1 US 9515707 W US9515707 W US 9515707W WO 9617041 A1 WO9617041 A1 WO 9617041A1
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- WIPO (PCT)
- Prior art keywords
- polymer
- olefin copolymer
- composition
- star
- crystalline
- Prior art date
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- 229920000642 polymer Polymers 0.000 title claims abstract description 189
- 229920000089 Cyclic olefin copolymer Polymers 0.000 title claims abstract description 96
- 229920002959 polymer blend Polymers 0.000 title claims abstract description 29
- 239000000203 mixture Substances 0.000 claims abstract description 151
- RRHGJUQNOFWUDK-UHFFFAOYSA-N Isoprene Chemical compound CC(=C)C=C RRHGJUQNOFWUDK-UHFFFAOYSA-N 0.000 claims abstract description 47
- 239000002270 dispersing agent Substances 0.000 claims abstract description 31
- 229920002943 EPDM rubber Polymers 0.000 claims abstract description 29
- 239000000654 additive Substances 0.000 claims abstract description 29
- 230000000996 additive effect Effects 0.000 claims abstract description 25
- 239000010687 lubricating oil Substances 0.000 claims abstract description 24
- 239000003963 antioxidant agent Substances 0.000 claims abstract description 13
- 230000003078 antioxidant effect Effects 0.000 claims abstract description 13
- 229920001577 copolymer Polymers 0.000 claims description 22
- 229920001195 polyisoprene Polymers 0.000 claims description 11
- 150000001336 alkenes Chemical class 0.000 claims description 2
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 claims description 2
- 235000006708 antioxidants Nutrition 0.000 claims 6
- 239000007787 solid Substances 0.000 abstract description 10
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 abstract description 8
- 239000003879 lubricant additive Substances 0.000 abstract description 7
- 239000000463 material Substances 0.000 abstract description 4
- HQQADJVZYDDRJT-UHFFFAOYSA-N ethene;prop-1-ene Chemical group C=C.CC=C HQQADJVZYDDRJT-UHFFFAOYSA-N 0.000 abstract description 2
- 125000000524 functional group Chemical group 0.000 abstract description 2
- 239000002480 mineral oil Substances 0.000 abstract description 2
- ROGIWVXWXZRRMZ-UHFFFAOYSA-N 2-methylbuta-1,3-diene;styrene Chemical compound CC(=C)C=C.C=CC1=CC=CC=C1 ROGIWVXWXZRRMZ-UHFFFAOYSA-N 0.000 abstract 1
- 239000000243 solution Substances 0.000 description 34
- 239000003921 oil Substances 0.000 description 25
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 15
- 239000005977 Ethylene Substances 0.000 description 15
- 238000000034 method Methods 0.000 description 15
- 239000002904 solvent Substances 0.000 description 11
- 150000001993 dienes Chemical class 0.000 description 10
- 239000000178 monomer Substances 0.000 description 10
- 229920001971 elastomer Polymers 0.000 description 9
- -1 maleic anhydride Chemical class 0.000 description 9
- 239000005060 rubber Substances 0.000 description 9
- 239000000523 sample Substances 0.000 description 9
- 238000013112 stability test Methods 0.000 description 9
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 description 8
- 238000003860 storage Methods 0.000 description 8
- 238000006243 chemical reaction Methods 0.000 description 7
- 230000000994 depressogenic effect Effects 0.000 description 7
- 239000012470 diluted sample Substances 0.000 description 7
- 239000010705 motor oil Substances 0.000 description 7
- 230000007935 neutral effect Effects 0.000 description 7
- 229920001897 terpolymer Polymers 0.000 description 7
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 6
- 239000002199 base oil Substances 0.000 description 6
- 238000009826 distribution Methods 0.000 description 6
- 238000012360 testing method Methods 0.000 description 6
- 239000013256 coordination polymer Substances 0.000 description 5
- 229920001038 ethylene copolymer Polymers 0.000 description 5
- 238000002360 preparation method Methods 0.000 description 5
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 5
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 5
- 230000008859 change Effects 0.000 description 4
- 239000000314 lubricant Substances 0.000 description 4
- 150000001875 compounds Chemical class 0.000 description 3
- 238000004090 dissolution Methods 0.000 description 3
- 238000001704 evaporation Methods 0.000 description 3
- 230000008020 evaporation Effects 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 230000000704 physical effect Effects 0.000 description 3
- SDJHPPZKZZWAKF-UHFFFAOYSA-N 2,3-dimethylbuta-1,3-diene Chemical compound CC(=C)C(C)=C SDJHPPZKZZWAKF-UHFFFAOYSA-N 0.000 description 2
- WHNWPMSKXPGLAX-UHFFFAOYSA-N N-Vinyl-2-pyrrolidone Chemical compound C=CN1CCCC1=O WHNWPMSKXPGLAX-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 125000003342 alkenyl group Chemical group 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000013329 compounding Methods 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000011156 evaluation Methods 0.000 description 2
- 239000003999 initiator Substances 0.000 description 2
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 230000009257 reactivity Effects 0.000 description 2
- 238000010992 reflux Methods 0.000 description 2
- 230000008719 thickening Effects 0.000 description 2
- AHAREKHAZNPPMI-AATRIKPKSA-N (3e)-hexa-1,3-diene Chemical compound CC\C=C\C=C AHAREKHAZNPPMI-AATRIKPKSA-N 0.000 description 1
- NVZWEEGUWXZOKI-UHFFFAOYSA-N 1-ethenyl-2-methylbenzene Chemical compound CC1=CC=CC=C1C=C NVZWEEGUWXZOKI-UHFFFAOYSA-N 0.000 description 1
- JZHGRUMIRATHIU-UHFFFAOYSA-N 1-ethenyl-3-methylbenzene Chemical compound CC1=CC=CC(C=C)=C1 JZHGRUMIRATHIU-UHFFFAOYSA-N 0.000 description 1
- DXIJHCSGLOHNES-UHFFFAOYSA-N 3,3-dimethylbut-1-enylbenzene Chemical compound CC(C)(C)C=CC1=CC=CC=C1 DXIJHCSGLOHNES-UHFFFAOYSA-N 0.000 description 1
- JLBJTVDPSNHSKJ-UHFFFAOYSA-N 4-Methylstyrene Chemical compound CC1=CC=C(C=C)C=C1 JLBJTVDPSNHSKJ-UHFFFAOYSA-N 0.000 description 1
- CTIIHLLLFSJVCN-UHFFFAOYSA-N 4-ethylhexa-1,3-diene Chemical compound CCC(CC)=CC=C CTIIHLLLFSJVCN-UHFFFAOYSA-N 0.000 description 1
- UGWOAPBVIGCNOV-UHFFFAOYSA-N 5-ethenyldec-5-ene Chemical compound CCCCC=C(C=C)CCCC UGWOAPBVIGCNOV-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 1
- 229920000181 Ethylene propylene rubber Polymers 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 235000011449 Rosa Nutrition 0.000 description 1
- 239000008186 active pharmaceutical agent Substances 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- XYLMUPLGERFSHI-UHFFFAOYSA-N alpha-Methylstyrene Chemical compound CC(=C)C1=CC=CC=C1 XYLMUPLGERFSHI-UHFFFAOYSA-N 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 229920006125 amorphous polymer Polymers 0.000 description 1
- 238000010539 anionic addition polymerization reaction Methods 0.000 description 1
- 150000001491 aromatic compounds Chemical class 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000007822 coupling agent Substances 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 239000002178 crystalline material Substances 0.000 description 1
- 239000004148 curcumin Substances 0.000 description 1
- 239000010710 diesel engine oil Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 125000006575 electron-withdrawing group Chemical group 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000011256 inorganic filler Substances 0.000 description 1
- 229910003475 inorganic filler Inorganic materials 0.000 description 1
- 239000010445 mica Substances 0.000 description 1
- 229910052618 mica group Inorganic materials 0.000 description 1
- 239000010688 mineral lubricating oil Substances 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- ATGUVEKSASEFFO-UHFFFAOYSA-N p-aminodiphenylamine Chemical compound C1=CC(N)=CC=C1NC1=CC=CC=C1 ATGUVEKSASEFFO-UHFFFAOYSA-N 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- UCMSRHPIFRZHDO-UHFFFAOYSA-N penta-1,3-diene Chemical compound CC=CC=C.CC=CC=C UCMSRHPIFRZHDO-UHFFFAOYSA-N 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 150000003254 radicals Chemical class 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000000454 talc Substances 0.000 description 1
- 229910052623 talc Inorganic materials 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
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- C10M157/00—Lubricating compositions characterised by the additive being a mixture of two or more macromolecular compounds covered by more than one of the main groups C10M143/00 - C10M155/00, each of these compounds being essential
- C10M157/04—Lubricating compositions characterised by the additive being a mixture of two or more macromolecular compounds covered by more than one of the main groups C10M143/00 - C10M155/00, each of these compounds being essential at least one of them being a nitrogen-containing compound
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- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
- C08L23/16—Ethene-propene or ethene-propene-diene copolymers
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- C10N2040/25—Internal-combustion engines
- C10N2040/255—Gasoline engines
- C10N2040/28—Rotary engines
-
- 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
- C10N2070/00—Specific manufacturing methods for lubricant compositions
- C10N2070/02—Concentrating of additives
Definitions
- This invention relates to additive compositions. Specifically, the present invention relates to additives which are blends of either crystalline olefin copolymers and star branched polymers or amorphous olefin copolymers and star branched polymers or blends of crystalline and amorphous olefin copolymers with star branched polymers.
- Lubricating oil compositions which use ethylene- propylene copolymer (EPM) or ethylene-propylene diene terpolymer (EPDM) as viscosity index improvers are known in the art. It is also known that such polymers can be amorphous or partly crystalline based on their ethylene/propylene content. Typically, random EPMs or EPDMs containing 40-70 mole % ethylene are amorphous, while copolymers or terpolymers containing over 70 mole % ethylene are partly crystalline. The crystallinity increases with the amount of ethylene.
- EPM ethylene- propylene copolymer
- EPDM ethylene-propylene diene terpolymer
- Linear amorphous polymers can flow under ambient conditions while the crystalline materials have excellent dimensional stability.
- solutions of partially crystalline olefin copolymers (OCPs) behave differently from amorphous OCPs as they can form ordered aggregates which tend to reduce viscosity.
- Lubricating oils containing neat, partially crystalline OCPs show improvement over conventional amorphous OCPs in low temperature cranking or pumbability performance, but their pour points are not satisfactory.
- VI improvers by contrast to amorphous OCP polymer VI improvers, the VI improvers based on partially crystalline OCPs require elevated temperatures for handling and storage as well as special blending conditions to achieve satisfactory performance.
- compositions comprising blends of at least one olefin copolymer and at least one star polymer. Additionally, the instant invention encompasses lubricating oil compositions comprising a mixture of base oil and the present polymer blends.
- compositions falling within the scope of the present invention can be dimensionally stable, and enhance the low temperature properties of a lubricating oil composition to which they have been added, and improve the viscosity index of lubricating oil.
- the present invention comprises lubricating oil composition containing a major portion of a lubricating oil (base oil) and minor amounts of a lubricant additive composition comprising crystalline olefin copolymers and star polymers or amorphous olefin copolymers and star polymers or a mixture of crystalline and amorphous olefin copolymers with star polymers.
- base oil a lubricating oil
- a lubricant additive composition comprising crystalline olefin copolymers and star polymers or amorphous olefin copolymers and star polymers or a mixture of crystalline and amorphous olefin copolymers with star polymers.
- the present invention relates to dimensionally stable blends of linear crystalline OCPs with star polymers or dimensionally stable crystalline and amorphous OCPs with star polymers or amorphous OCPs with star polymers which are useful for VI improver applications in lubricant oil compositions.
- These polymeric blends exhibit the desirable properties of their individual components but reduce or eliminate their undesirable properties.
- Blends of crystalline OCPs and star polymers as well as blends of crystalline and amorphous OCPs with star polymers exhibit dimensional stability and also provide lubricating oil compositions which have a high degree of shear stability and exhibit enhanced low temperature properties.
- the blend of amorphous OCPs and star polymers can be used in lubricant oil compositions to provide lubricant oil compositions with desirable properties such as good shear stability and enhanced low temperature property.
- the novel polymer blend may comprise an oil- soluble composition comprising a star polymer and an amorphous copolymer (random EPM or EPDM) wherein the copolymer or terpolymer has an ethylene content from 40 to 70 mole %, and a partially crystalline copolymer or terpolymer having an ethylene content from above 70 to 85 mole%. It may also comprise a star polymer and a partially crystalline olefin copolymer or terpolymer having an ethylene content from above 70 to 85% mole and a star polymer.
- an oil- soluble composition comprising a star polymer and an amorphous copolymer (random EPM or EPDM) wherein the copolymer or terpolymer has an ethylene content from 40 to 70 mole %, and a partially crystalline copolymer or terpolymer having an ethylene content from above 70 to 85 mole%. It may also comprise a star polymer and a partially crystalline o
- the amorphous and crystalline copolymer and terpolymers may be prepared using known Ziegler-Natta polymerization methods. Ethylene-propylene copolymers (EPM) and ethylene-propylene-diene terpolymers (EPDM) with and without polar groups attached to the main polymeric chain are preferred for the purpose of this invention.
- EPM Ethylene-propylene copolymers
- EPDM ethylene-propylene-diene terpolymers
- the unsaturated monomers (third monomers) used for the preparation of terpolymers are preferably linear, but may be branched. The amount of the third monomer contained in the terpolymer may range from 0.01 to about 10 weight %.
- polymeric additive compositions also comprise blends analogous to those mentioned hereinabove in which amorphous EPM or EPDM with attached polar functional groups are employed.
- EPM and EPDM with attached polar groups include but are not limited to all known dispersant olefin copolymers (DOCP) or dispersant antioxidant olefin copolymers (DAOCP) .
- DOCP and DAOCP are known to workers in the field as exemplified in De Rosa et al U.S. Patents 5,013,469 and 5,112,508 and Kapuscinski et al. U.S. Patent 5,094,766 herein incorporated by reference.
- the DAOCP and DOCP polymers may be part of or the only OCP used in the lubricant additive mixture of this invention.
- blends of DOCP with other OCP's or blends of DAOCP with other OCP's may be used.
- Preferred blends are about 10 to 70% amorphous OCPs and about 90 to 30% DOCP or about 90 to 30% DAOCP.
- Most preferred blends are about 30 to 60% of OCPs and about 70 to 40% DOCP or about 70 to 40% DAOCP.
- Star polymers are known and can be prepared by anionic polymerization methods as exemplified by Rhodes et al. U.S. Patent 5,035,820 and Echert, U.S. Patent 4,358,565, which are herein incorporated by reference. These polymers generally produced by the process comprising the following reaction steps:
- the star polymer may be hydrogenated.
- the living polymers obtained by reaction step (a), which are linear unsaturated living polymers, are prepared from one or more conjugated dienes, e.g., C 4 to C, j conjugated dienes and, optionally, one or more 1 monoalkenyl arene compounds.
- conjugated dienes include butadiene (1,3-butadiene) ; isoprene, 1,3- pentadiene (piperylene) ; 2,3-dimethyl-1,3-butadiene; 3- butyl-1,3-octadiene, 1-phenyl-l,3-butadiene; 1,3- hexadiene; and 4-ethyl-1,3-hexadiene with butadiene and/or isoprene being preferred.
- the living polymers may also be partly derived from one or more monoalkenyl arene compounds.
- Preferred monoalkenyl arene compounds are the monovinyl aromatic compounds such as styrene, monovinylnapthalene as well as the alkylated derivatives thereof such as o-, m- and p-methylstyrene, alpha-methylstyrene and tertiary- butylstyrene.
- Styrene is the preferred monoalkenyl arene compound.
- the living polymers produced in reaction step (a) are then reacted, in reaction step (b) , with a polyalkenyl compounding agent.
- Polyalkyl compounding agents capable of forming star-shaped polymers are known. See generally, Fetters et al., U.S. Pat. No. 3,985,830; Milovich, Canadian Pat. No. 716,645; and British Pat. No. 1,025,295. They are usually compounds having at least two non-conjugated alkenyl groups. Such groups are usually attached to the same or different electron withdrawing groups, e.g., an aromatic nucleus. Such compounds have the property that at least two of the alkenyl groups are capable of independent reaction with different living polymers.
- star polymers are star branched hydrogenated isoprenes.
- Hydrogenated star branched isoprene are commercially available.
- Examples of commercially available hydrogenated star branched isoprenes polymers that can be used in the instant compositions include, but are not limited to, the SHELLVIS 200 series, such as SHELLVIS 250, SHELLVIS 200, and SHELLVIS 260.
- Solid polymer blends comprising shear stable and/or non shear stable partially crystalline linear olefin copolymers with star polymers have been found to give good dimensional stability, excellent shear stability and satisfactory solubility in mineral oils.
- the present polymer additive blends are viscosity index improvers and provide improved low temperature properties to motor oils and do not show adverse reactivity with other components.
- the aforementioned additive polymer compositions may be added to a major portion of lubricating oil (base oil) resulting in a composition comprising a major portion of lubricating oil (base oil) and a minor portion of lubricant additive composition. With respect to the present invention a major portion is considered to be 80- 90 wt % while a minor portion is 1-20 wt %.
- One embodiment of this invention relates to polymeric additive compositions comprising a mixture of at least one crystalline ethylene-propylene copolymer (EPM) or ethylene-propylene-diene terpolymer (EPDM) with at least one star polymer which are useful for preparing shear stable VI improvers.
- EPM crystalline ethylene-propylene copolymer
- EPDM ethylene-propylene-diene terpolymer
- star polymer which are useful for preparing shear stable VI improvers.
- the instant blends show good dimensional stability when they preferably contain at least about 10 wt % of a crystalline OCP component.
- Preferred blends of crystalline OCPs and star polymers comprise from about 10 to 70 wt% crystalline OCP and from about 90 to 30 wt% star polymers, most preferred are about 20 to 60 wt% crystalline OCPs and about 80 to 40 wt% star polymers, most preferable are about 30 to 50 wt% crystalline OCPs and about 70 to 50 % star polymers.
- Yet another embodiment of this invention relates to a lubricant additive composition, comprising a mixture of at least one amorphous and at least one crystalline olefin copolymers with at least one star polymer.
- Preferred blends comprise about 30 % crystalline OCP, about 50 % amorphous OCP and 20 % star polymers. More preferably about 20 to 60% crystalline OCP, about 30 to 70% amorphous OCP and 10 to 50% star polymers and most preferred is 30 to 50% OCP 20 to 40% amorphous OCP and 10 to 30 star polymers.
- the instant lubricant additive blends which include a crystalline olefin are easily shippable as solids and retain their dimensional stability.
- compositions comprising amorphous EPM or EPDM with star polymers.
- Preferred blends comprises about 10 to 90wt% amorphous OCPs and 90 to 10wt% star polymers. Most preferred is about 20 to 60wt% amorphous OCPs and about 80 to 40 wt% star" polymer. Most preferable is about 30 to 50 wt% amorphous OCPs and 70 to 50wt% star polymer. Compared to neat amorphous OCP, these blends provide enhanced low temperature properties in motor oils.
- the blends can be prepared by various conventional methods such as by devolatilization of blended polymer solutions or by blending of the solid rubbers in the mastificator, Brabender mixer or extruder.
- One method is to mix solutions of the polymers and then to devolatilize the mixed solutions to produce a solid polymer blend.
- Another method is to mix solid polymers, referred to as rubbers, in a masticator, the Brabender Mixer, or an extruder. In the solution/devolatilization procedure, the solvent from the solution of the copolymer rubbers is removed by evaporation.
- Oil concentrates of the dimensionally stable polymer blend are prepared as follows:
- a base oil or a mineral lubricating oil or synthetic oil is heated to 80-300°F in a vessel equipped with a mechanical stirrer and a heating jacket.
- Pieces of the polymer blend are charged gradually to the oil forming a mixture.
- the mixture is stirred at 80-300°F until the rubber is completely dissolved, which may require from 1-24 hours.
- the polymer content may be adjusted to a required viscosity level.
- Lubricating oils in which the multifunctional additives of this invention may find use may include automotive, aircraft, marine, railway, etc., oils; oils used in spark ignition or compression ignition; summer or winter oils, etc.
- the lubricating oils may be characterized by a b.p. of about 570 ⁇ F. to about 660°F., preferably 610°F., an e.p. of about 750°F. to about 1200°F., preferably 1020 ⁇ F.; an API gravity of about 25 to about 31, preferably about 29.
- a typical lubricating oil in which the polymer of this invention may be present may be automotive or diesel engine oil.
- the polymer blends of the invention show good dimensional stability and the performance of these blends provide enhanced low temperature (cold cranking) performance in motor oils, good pour points, and satisfactory cold storage properties.
- Pieces of various polymers ( ⁇ i n cubes) are charged gradually to a mixer fitted with a reflux condenser and containing a low boiling hydrocarbon solvent, typically n-hexane, cyclohexane or n-heptane.
- a low boiling hydrocarbon solvent typically n-hexane, cyclohexane or n-heptane.
- the mixture is stirred at 60 to 80 C until the rubbers are completely dissolved (approx. 8 hours)
- the solvent is removed by evaporation under vacuum.
- the polymer blend residue is tested for dimensional stability and the solution properties in oil are examined.
- the equipment and dissolution procedure typically used for the manufacture of OCP VI improvers from solid rubber is used for the preparation of the VI improvers from polymer blends:
- Base oil is heated to 80 - 300 F in a mixer equipped with a mechanical stirrer and heating jacket.
- Pieces of polymer blend ( ⁇ #" cubes) are charged gradually to the mixer.
- the mixture is stirred to 80 to 300 F until the rubber is completely dissolved (approx. 1 - 24 hours) .
- the polymer content is adjusted to the required viscosity level. It can vary with molecular weight of the polymer and blend composition.
- the resulting concentrated solution is used "as is” for further testing.
- Polymers are dissolved in n-heptane at 60 C for 8 hours at a temperature of 150 F in a mixer equipped with a mechanical stirrer, reflux condenser and heating jacket. Following complete dissolution of the polymers, the heptane is removed by evaporation under vacuum. A 1" cube is formed from the polymer blend residue and cooled to room temperature.
- a l" cube of solid rubber is placed between two 3" x C aluminum plates at ambient temperature.
- the change in the dimensions of the polymer with time is observed and described as follows: excellent - no change good - slight change fair - significant change poor - flows
- Standard Texaco or ASTM test methods were used for the evaluation of the physical properties of the VI improvers.
- SSI Shear Stability Index
- Vbs - Vas x l00% TP Vbs - Vas x l00% TP
- TP is the thickening power measured by the difference between Vbs and solvent viscosity.
- Vbs - Vas x 100% is viscosity loss determined VBS according to the ASTM Method D-3945 (Proc. A) .
- Bench Dispersancv
- sample VI improver is blended into a formulated oil, which does not contain a dispersant, to make a 10 wt% VI improver solution.
- the blend is then tested for dispersancy in the Bench VE Test.
- the evaluation of the cold storage behavior of VI improvers and motor oils containing them was made by utilizing the Ultra Low Temperature Environmental Chamber (Thermotron S-8C) . This piece of equipment allows the determination of the stability of materials under cold temperature conditions. Such conditions were simulated by programming temperatures between -60 and 4 deg. F using an 18 hour time cycle. The samples were examined at 10 degrees Fahrenheit after 8 weeks of storage under these conditions.
- Thermotron S-8C Ultra Low Temperature Environmental Chamber
- Polymer blends were prepared using different ratios of a partially crystalline ethylene copolymer, amorphous ethylene copolymer and star isoprenes, SHELLVIS 250 or SHELLVIS 200. The components used and their properties are listed in Table I.
- Polymer A is a blend consisting of 40 wt% of partially crystalline ethylene-propylene-diene terpolymer containing approximately 77-80 mole % ethylene, about 0.1- 1.0 weight percent diene monomer, with the balance being propylene, and 60 wt% of amorphous ethylene-propylene diene terpolymer containing 56-62 mole % ethylene, about 0.1-0.5 weight percent diene monomer and the balance propylene.
- Polvmer B is a commercial polymer, SHELLVIS 250, having a star branch structure with polyisoprene branches attached to a central core.
- Polvmer C is a commercial polymer, SHELLVIS 200, having a star branch structure with polyisoprene branches attached to a central core. The molecular weight of this polymer is lower than that of Polvmer B.
- Polymer D is a partially crystalline ethylene- propylene-diene terpolymer containing approximately 77-80 mole % ethylene, about 0.1-1.0 weight percent diene monomer, and the balance propylene.
- Polymer E is an amorphous ethylene-propylene- diene terpolymer containing 56-62 mole % ethylene, about 0.1-1.0 weight percent piece monomer, and the balance propylene.
- Polymer F is a blend consisting of 20 wt% of partially crystalline ethylene-propylene-diene terpolymer containing approximately 77-80 mole % ethylene, about 0.1- 1.0 weight percent diene monomer, and the balance propylene, and of 80 wt% dispersant amorphous ethylene- propylene-diene terpolymer containing 56-62 mole % ethylene, and about 2 wt% of pendant units derivatized from N-vinylpyrrolidone.
- a number average molecular weight as measured by GPC is approximately 70,000, a molecular weight distributions of approximately 2.01, and a crystallinity of about 3%.
- Polvmer G is a dispersant amorphous ethylene- propylene-diene terpolymer containing 56-62 mole % ethylene, about 0.1-1.0 weight percent diene monomer, and about 2 wt% of pendant units derivatized from N- vinylpyrrolidone.
- a number average molecular weight as measured by GPC is approximately 70,000, a molecular weight distribution of approximately 2.1.
- Polymer H is a dispersant/antioxidant amorphous ethylene-propylene copolymer containing 56-62 mole % ethylene, and about 1 wt% of pendant units derivatized from maleic anhydride and N-phenyl-p-phenylenediamine.
- Polymer blends were prepared using different ratios of a partially crystalline ethylene copolymer blend, designated Polvmer A, and of star polymer (SHELLVIS 250) designated Polymer B. The resulting blends were tested for dimensional stability in the Dimensional Stability Test and for shear stability in the Shear Stability test. The results were compared to the individual polymers: Polymer A and Polvmer B (Table II)
- Polymer blends were prepared using different ratios of a partially crystalline ethylene copolymer blend, designated Polymer A, and of star polymer (SHELLVIS 200) designated Polymer C. The resulting blends were tested for dimensional stability in the Dimensional Stability Test and shear stability in the Shear Stability test. The results were compared to the individual polymers: Polymer A and Polymer C (Table III)
- Polymer blends were prepared using 60 wt% of a partially crystalline ethylene copolymer, designated Polymer D, and 40 wt% of star polymer (SHELLVIS 250) designated Polymer B. The resulting blends were tested for dimensional stability in the Dimensional Stability Test. The Shear Stability Index was calculated from the blend components. The results were compared to the individual polymers: Polymer D and Polymer B (Table IV) Tftble IV, SAMPLES OF EXAMPLE III
- Polymer blends were prepared using 60 wt% of a amorphous OCP designated Polymer E, and 40 wt% of star polymer (SHELLVIS 250) designated Polymer B. The resulting blends were tested for dimensional stability in the Dimensional Stability Test. The Shear Stability Index was calculated from the blend components. The results were compared to the individual polymers: Polymer E and Polymer B (Table V)
- Polymer blends were prepared using 80 and 90 wt% of a dispersant crystalline OCP blend, designated Polymer F, and the balance of star polymer (SHELLVIS 250) designated Polymer B. The resulting blends were tested for dimensional stability in the Dimensional Stability Test. The shear stability was calculated from the blend components. The results were compared to the individual polymers: Polymer F and Polymer B (Table VI) Table VI. SAMPLES OF EXAMPLE V
- Polymer blends were prepared using 80 wt% of a dispersant amorphous OCP, designated Polymer G, and 20 wt% of star polymer (SHELLVIS 250) designated Polymer B. The resulting blends were tested for dimensional stability in the Dimensional Stability Test. The shear stability was calculated from the blend components. The results were compared to the individual polymers: Polymer G and Polymer B (Table VII)
- Polymer blends were prepared using 80 wt% of a dispersant/antioxidant amorphous OCP, designated Polymer H, and 20 wt% of star polymer (SHELLVIS 250) designated Polymer B. The resulting blends were tested for dimensional stability in the Dimensional Stability Test. The shear stability was calculated from the blend components. The results were compared to the individual polymers: Polymer H and Polymer B (Table VIII) Table VIII. SAMPLES OF EXAMPLE VII
- the blends containing star polyisoprene give products with significantly better pour points and Brookfield Viscosities.
- the appearance during the extended cold storage is satisfactory for both neat VI improvers and fully formulated oils containing them.
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Health & Medical Sciences (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Lubricants (AREA)
Abstract
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AU45072/96A AU4507296A (en) | 1994-12-02 | 1995-12-04 | Polymer blends containing olefin copolymers and star branched polymers |
| EP95943653A EP0794995A1 (fr) | 1994-12-02 | 1995-12-04 | Melanges polymeres contenant des copolymeres d'olefines et des polymeres ramifies en etoile |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US34845594A | 1994-12-02 | 1994-12-02 | |
| US08/348,455 | 1994-12-02 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO1996017041A1 true WO1996017041A1 (fr) | 1996-06-06 |
Family
ID=23368123
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/US1995/015707 WO1996017041A1 (fr) | 1994-12-02 | 1995-12-04 | Melanges polymeres contenant des copolymeres d'olefines et des polymeres ramifies en etoile |
Country Status (3)
| Country | Link |
|---|---|
| EP (1) | EP0794995A1 (fr) |
| AU (1) | AU4507296A (fr) |
| WO (1) | WO1996017041A1 (fr) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2002010276A3 (en) * | 2000-07-31 | 2002-04-25 | Lubrizol Corp | Polymeric mixture useful as viscosity improver for lubricating oils |
| EP1632504A3 (fr) * | 2004-08-27 | 2006-06-07 | Polimeri Europa S.p.A. | Copolymères à base d'éthylène et propylène ayant une stabilité de forme améliorée et utilisables pour modifier des huiles lubrifiantes et procédé de préparation de ceux-ci |
| WO2007093446A1 (fr) * | 2006-02-16 | 2007-08-23 | Polimeri Europa S.P.A. | Copolymères éthylène-propylène adaptés à la modification d'huiles lubrifiantes et procédé de synthèse desdits copolymères |
| EP1925657A3 (fr) * | 2006-10-10 | 2010-03-31 | Infineum International Limited | Compositions d'huile lubrifiante |
| US7776804B2 (en) | 2005-03-16 | 2010-08-17 | The Lubrizol Corporation | Viscosity improver compositions providing improved low temperature characteristics to lubricating oil |
| WO2011029580A1 (fr) | 2009-09-08 | 2011-03-17 | Unilever Plc | Utilisation de copolymères ramifiés dans des mélanges de polymères |
| US8188021B2 (en) | 2005-11-04 | 2012-05-29 | Infineum International Limited | Lubricating oil compositions |
| CN105273816A (zh) * | 2015-10-16 | 2016-01-27 | 大连创达技术交易市场有限公司 | 一种具有抗高温蒸发的合成发动机润滑油 |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1337475A (en) * | 1970-06-02 | 1973-11-14 | Exxon Research Engineering Co | Lubricant containing ethylene/alphaolefin copolymers |
| FR2391268A2 (fr) * | 1977-05-19 | 1978-12-15 | Orobis Ltd | Composition a base d'un copolymere sequence et d'un autre copolymere, destinee a ameliorer l'indice de viscosite d'une huile lubrifiante, et composition lubrifiante formulee comportant cet additif |
| US4833194A (en) * | 1987-11-13 | 1989-05-23 | R.J.F. International Corporation | Elastomeric thermoplastic compositions |
| EP0452813A2 (fr) * | 1990-04-12 | 1991-10-23 | UNION CARBIDE CHEMICALS AND PLASTICS COMPANY INC. (a New York corporation) | Procédé pour le moulage à froid de copolymères de propylène |
| EP0555930A2 (fr) * | 1992-02-13 | 1993-08-18 | Shell Internationale Researchmaatschappij B.V. | Formulations de revêtement de sol et de mur |
-
1995
- 1995-12-04 AU AU45072/96A patent/AU4507296A/en not_active Abandoned
- 1995-12-04 EP EP95943653A patent/EP0794995A1/fr not_active Withdrawn
- 1995-12-04 WO PCT/US1995/015707 patent/WO1996017041A1/fr not_active Application Discontinuation
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1337475A (en) * | 1970-06-02 | 1973-11-14 | Exxon Research Engineering Co | Lubricant containing ethylene/alphaolefin copolymers |
| FR2391268A2 (fr) * | 1977-05-19 | 1978-12-15 | Orobis Ltd | Composition a base d'un copolymere sequence et d'un autre copolymere, destinee a ameliorer l'indice de viscosite d'une huile lubrifiante, et composition lubrifiante formulee comportant cet additif |
| US4833194A (en) * | 1987-11-13 | 1989-05-23 | R.J.F. International Corporation | Elastomeric thermoplastic compositions |
| EP0452813A2 (fr) * | 1990-04-12 | 1991-10-23 | UNION CARBIDE CHEMICALS AND PLASTICS COMPANY INC. (a New York corporation) | Procédé pour le moulage à froid de copolymères de propylène |
| EP0555930A2 (fr) * | 1992-02-13 | 1993-08-18 | Shell Internationale Researchmaatschappij B.V. | Formulations de revêtement de sol et de mur |
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2002010276A3 (en) * | 2000-07-31 | 2002-04-25 | Lubrizol Corp | Polymeric mixture useful as viscosity improver for lubricating oils |
| US8524645B2 (en) | 2003-03-28 | 2013-09-03 | The Lubrizol Corporation | Viscosity improver compositions providing improved low temperature characteristics to lubricating oil |
| EP1632504A3 (fr) * | 2004-08-27 | 2006-06-07 | Polimeri Europa S.p.A. | Copolymères à base d'éthylène et propylène ayant une stabilité de forme améliorée et utilisables pour modifier des huiles lubrifiantes et procédé de préparation de ceux-ci |
| US7208543B2 (en) | 2004-08-27 | 2007-04-24 | Polimeri Europa S.P.A. | Ethylene-propylene copolymers with an improved shape stability suitable for modifying lubricating oils and process for the preparation thereof |
| US7776804B2 (en) | 2005-03-16 | 2010-08-17 | The Lubrizol Corporation | Viscosity improver compositions providing improved low temperature characteristics to lubricating oil |
| US8188021B2 (en) | 2005-11-04 | 2012-05-29 | Infineum International Limited | Lubricating oil compositions |
| WO2007093446A1 (fr) * | 2006-02-16 | 2007-08-23 | Polimeri Europa S.P.A. | Copolymères éthylène-propylène adaptés à la modification d'huiles lubrifiantes et procédé de synthèse desdits copolymères |
| RU2430962C2 (ru) * | 2006-02-16 | 2011-10-10 | Полимери Эуропа С.П.А. | Сополимеры этилена и пропилена, пригодные для модифицирования смазочных масел, и способ их получения |
| US8193135B2 (en) | 2006-02-16 | 2012-06-05 | Polimeri Europa S.P.A. | Ethylene-propylene copolymers suitable for the modification of lubricating oils and process for the preparation thereof |
| EP1925657A3 (fr) * | 2006-10-10 | 2010-03-31 | Infineum International Limited | Compositions d'huile lubrifiante |
| WO2011029580A1 (fr) | 2009-09-08 | 2011-03-17 | Unilever Plc | Utilisation de copolymères ramifiés dans des mélanges de polymères |
| CN105273816A (zh) * | 2015-10-16 | 2016-01-27 | 大连创达技术交易市场有限公司 | 一种具有抗高温蒸发的合成发动机润滑油 |
Also Published As
| Publication number | Publication date |
|---|---|
| AU4507296A (en) | 1996-06-19 |
| EP0794995A1 (fr) | 1997-09-17 |
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