CN101319163A - Lubricating oil composition for internal combustion engine - Google Patents
Lubricating oil composition for internal combustion engine Download PDFInfo
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- CN101319163A CN101319163A CNA2008100982508A CN200810098250A CN101319163A CN 101319163 A CN101319163 A CN 101319163A CN A2008100982508 A CNA2008100982508 A CN A2008100982508A CN 200810098250 A CN200810098250 A CN 200810098250A CN 101319163 A CN101319163 A CN 101319163A
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- 239000010687 lubricating oil Substances 0.000 title claims abstract description 46
- 239000000203 mixture Substances 0.000 title claims abstract description 46
- 238000002485 combustion reaction Methods 0.000 title claims abstract description 37
- KHYKFSXXGRUKRE-UHFFFAOYSA-J molybdenum(4+) tetracarbamodithioate Chemical compound C(N)([S-])=S.[Mo+4].C(N)([S-])=S.C(N)([S-])=S.C(N)([S-])=S KHYKFSXXGRUKRE-UHFFFAOYSA-J 0.000 claims abstract description 32
- 239000000654 additive Substances 0.000 claims abstract description 23
- 239000002199 base oil Substances 0.000 claims abstract description 23
- 229910052751 metal Inorganic materials 0.000 claims abstract description 18
- 239000002184 metal Substances 0.000 claims abstract description 18
- 230000000996 additive effect Effects 0.000 claims abstract description 14
- 239000003599 detergent Substances 0.000 claims abstract description 13
- 239000002480 mineral oil Substances 0.000 claims abstract description 11
- 235000010446 mineral oil Nutrition 0.000 claims abstract description 11
- 229910052784 alkaline earth metal Inorganic materials 0.000 claims description 19
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims description 13
- 229910052698 phosphorus Inorganic materials 0.000 claims description 13
- 239000011574 phosphorus Substances 0.000 claims description 13
- 150000001342 alkaline earth metals Chemical class 0.000 claims description 12
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 claims description 10
- 229910052750 molybdenum Inorganic materials 0.000 claims description 10
- 239000011733 molybdenum Substances 0.000 claims description 10
- 239000010705 motor oil Substances 0.000 abstract description 18
- 230000008021 deposition Effects 0.000 abstract description 13
- 230000001050 lubricating effect Effects 0.000 abstract description 4
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 abstract description 3
- 229910052725 zinc Inorganic materials 0.000 abstract description 3
- 239000011701 zinc Substances 0.000 abstract description 3
- 125000004119 disulfanediyl group Chemical group *SS* 0.000 abstract 1
- 239000004615 ingredient Substances 0.000 abstract 1
- -1 polyol esters Chemical class 0.000 description 19
- 150000001875 compounds Chemical class 0.000 description 15
- WMYJOZQKDZZHAC-UHFFFAOYSA-H trizinc;dioxido-sulfanylidene-sulfido-$l^{5}-phosphane Chemical compound [Zn+2].[Zn+2].[Zn+2].[O-]P([O-])([S-])=S.[O-]P([O-])([S-])=S WMYJOZQKDZZHAC-UHFFFAOYSA-H 0.000 description 14
- 239000003054 catalyst Substances 0.000 description 12
- 230000000052 comparative effect Effects 0.000 description 12
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- 125000000217 alkyl group Chemical group 0.000 description 10
- 239000003921 oil Substances 0.000 description 10
- 239000001993 wax Substances 0.000 description 10
- 239000000446 fuel Substances 0.000 description 9
- 239000002904 solvent Substances 0.000 description 8
- 229960002317 succinimide Drugs 0.000 description 7
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 6
- 125000003342 alkenyl group Chemical group 0.000 description 6
- 238000004517 catalytic hydrocracking Methods 0.000 description 6
- 239000001257 hydrogen Substances 0.000 description 6
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- 238000000034 method Methods 0.000 description 6
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- 125000004432 carbon atom Chemical group C* 0.000 description 5
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- VQTUBCCKSQIDNK-UHFFFAOYSA-N Isobutene Chemical compound CC(C)=C VQTUBCCKSQIDNK-UHFFFAOYSA-N 0.000 description 4
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- 238000009835 boiling Methods 0.000 description 4
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- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 3
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- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
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- 125000004434 sulfur atom Chemical group 0.000 description 3
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- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 2
- ZJCCRDAZUWHFQH-UHFFFAOYSA-N Trimethylolpropane Chemical compound CCC(CO)(CO)CO ZJCCRDAZUWHFQH-UHFFFAOYSA-N 0.000 description 2
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- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 description 2
- KGBXLFKZBHKPEV-UHFFFAOYSA-N boric acid Chemical compound OB(O)O KGBXLFKZBHKPEV-UHFFFAOYSA-N 0.000 description 2
- 239000004327 boric acid Substances 0.000 description 2
- 150000001639 boron compounds Chemical class 0.000 description 2
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 2
- 229910017052 cobalt Inorganic materials 0.000 description 2
- 239000010941 cobalt Substances 0.000 description 2
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 2
- 238000004508 fractional distillation Methods 0.000 description 2
- 239000000295 fuel oil Substances 0.000 description 2
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- 239000011777 magnesium Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 229910052759 nickel Inorganic materials 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000007670 refining Methods 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 229910052717 sulfur Inorganic materials 0.000 description 2
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 2
- 229910052721 tungsten Inorganic materials 0.000 description 2
- 239000010937 tungsten Substances 0.000 description 2
- GDGUCRQNTDPGSD-UHFFFAOYSA-N 2,2-bis(hydroxymethyl)propane-1,3-diol Chemical compound OCC(CO)(CO)CO.OCC(CO)(CO)CO GDGUCRQNTDPGSD-UHFFFAOYSA-N 0.000 description 1
- FALRKNHUBBKYCC-UHFFFAOYSA-N 2-(chloromethyl)pyridine-3-carbonitrile Chemical group ClCC1=NC=CC=C1C#N FALRKNHUBBKYCC-UHFFFAOYSA-N 0.000 description 1
- 229910015900 BF3 Inorganic materials 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-M Bisulfite Chemical compound OS([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-M 0.000 description 1
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- YGSDEFSMJLZEOE-UHFFFAOYSA-N Salicylic acid Natural products OC(=O)C1=CC=CC=C1O YGSDEFSMJLZEOE-UHFFFAOYSA-N 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 235000011037 adipic acid Nutrition 0.000 description 1
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- 150000001298 alcohols Chemical class 0.000 description 1
- 150000001299 aldehydes Chemical class 0.000 description 1
- 125000002877 alkyl aryl group Chemical group 0.000 description 1
- 125000005119 alkyl cycloalkyl group Chemical group 0.000 description 1
- AZDRQVAHHNSJOQ-UHFFFAOYSA-N alumane Chemical class [AlH3] AZDRQVAHHNSJOQ-UHFFFAOYSA-N 0.000 description 1
- 125000003368 amide group Chemical group 0.000 description 1
- 125000003277 amino group Chemical group 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 239000002518 antifoaming agent Substances 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910052796 boron Inorganic materials 0.000 description 1
- WTEOIRVLGSZEPR-UHFFFAOYSA-N boron trifluoride Chemical compound FB(F)F WTEOIRVLGSZEPR-UHFFFAOYSA-N 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000012459 cleaning agent Substances 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 150000005676 cyclic carbonates Chemical class 0.000 description 1
- 230000000994 depressogenic effect Effects 0.000 description 1
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- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
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- SLCVBVWXLSEKPL-UHFFFAOYSA-N neopentyl glycol Chemical compound OCC(C)(C)CO SLCVBVWXLSEKPL-UHFFFAOYSA-N 0.000 description 1
- 125000004433 nitrogen atom Chemical group N* 0.000 description 1
- 125000002347 octyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
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- FJKROLUGYXJWQN-UHFFFAOYSA-N papa-hydroxy-benzoic acid Natural products OC(=O)C1=CC=C(O)C=C1 FJKROLUGYXJWQN-UHFFFAOYSA-N 0.000 description 1
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Abstract
Description
技术领域 technical field
本发明涉及一种内燃机用润滑油组合物,尤其是涉及一种高温沉积性能良好、并且低磨耗特性优异的长寿命节油型内燃机用润滑油组合物。The invention relates to a lubricating oil composition for an internal combustion engine, in particular to a long-life fuel-saving lubricating oil composition for an internal combustion engine with good high-temperature deposition performance and excellent low wear characteristics.
背景技术 Background technique
近年来,为了防止地球变暖,迫切要求提高汽车的燃油效率、抑制CO2的排放量。为了提高汽车的燃油效率,重要的是提高发动机(engine)的效率,汽油发动机(gasolineengine)一直采用稀燃(lean burn)、直喷(direct-injection)、或涡轮增压机(turbocharger)技术。另一方面,减小发动机的摩擦也能有助于提高燃油效率,因此对滑动零件使用低摩擦材料或者采用节油型发动机油。In recent years, in order to prevent global warming, it has been urgently required to improve the fuel efficiency of automobiles and to suppress CO 2 emissions. In order to improve the fuel efficiency of automobiles, it is important to improve the efficiency of the engine. Gasoline engines have always used lean burn, direct-injection, or turbocharger technologies. On the other hand, reducing friction in the engine can also help improve fuel efficiency, so use low-friction materials for sliding parts or use fuel-efficient engine oil.
已知,为了制造节油型发动机油(engine oil),下述方法较为有效:降低发动机油的粘度,使粘度达到美国汽车技术协会(Society of Automotive Engineers,SAE)J300所规定的粘度分类中的5W-20或0W-20,并调配减小摩擦的添加剂(摩擦调整剂,以下,有时也称为FM)即二硫代氨基甲酸钼(MoDTC)等有机钼系FM(参照K.Hoshino et al,Fuel Efficiency of SAE 5W-20 Friction Modified Gasoline Engine Oil,SAE Technical Paper982506(1998)、以及日本专利特开平10-17883号公报)。It is known that in order to manufacture fuel-saving engine oil (engine oil), the following method is more effective: reduce the viscosity of the engine oil, so that the viscosity reaches the viscosity classification specified by the American Society of Automotive Engineers (Society of Automotive Engineers, SAE) J300. 5W-20 or 0W-20, and the deployment of additives to reduce friction (friction modifier, hereinafter, sometimes also referred to as FM), that is, organic molybdenum-based FM such as molybdenum dithiocarbamate (MoDTC) (refer to K.Hoshino et al , Fuel Efficiency of SAE 5W-20 Friction Modified Gasoline Engine Oil, SAE Technical Paper 982506 (1998), and Japanese Patent Laid-Open Publication No. 10-17883).
另一方面,稀燃发动机及直喷发动机的效率比原来的发动机高,因此燃烧温度也有上升的趋势,使得活塞(piston)等曝露在更高的温度下。另外,涡轮增压机是将空气压缩并强制供给到气缸内,由此,虽然与排气量相同的非增压式发动机(Natural aspirationengine)相比,可以增大发动机的功率,但会使发动机一直曝露在高温下。因此,发动机油的高温沉积性能也必须得到提高。也就是说,要求今后的节油型发动机油的高温沉积性能优于原先的发动机油。On the other hand, lean-burn engines and direct-injection engines are more efficient than conventional engines, so the combustion temperature also tends to rise, exposing pistons and the like to higher temperatures. In addition, the turbocharger compresses the air and forcibly supplies it into the cylinder. Therefore, although the power of the engine can be increased compared with a non-supercharged engine (Natural aspiration engine) with the same displacement, it will make the engine Constantly exposed to high temperatures. Therefore, the high-temperature deposition performance of engine oil must also be improved. That is to say, future fuel-saving engine oils are required to have better high-temperature deposition performance than the original engine oils.
发明内容 Contents of the invention
鉴于以上状况,本发明的课题在于提供一种高温沉积性能优异、并且节油性优异的发动机油。In view of the above circumstances, an object of the present invention is to provide an engine oil having excellent high-temperature deposition performance and excellent fuel economy.
为了解决所述课题,本发明人进行了努力研究,结果发现,在矿物油以及/或者合成系基础油中调配特定量的碱土金属系清洁剂,并且以特定的比例调配特定量的二烷基二硫代磷酸锌(ZnDTP)和特定量的二硫代氨基甲酸钼(MoDTC)而制成的润滑油组合物可以用作高温沉积性能良好的节油型发动机油。本发明是根据该见解研制而成的。In order to solve the above-mentioned problems, the inventors of the present invention conducted diligent research and found that a specific amount of an alkaline earth metal-based detergent is blended in a mineral oil and/or a synthetic base oil, and a specific amount of a dialkyl detergent is blended in a specific ratio. The lubricating oil composition prepared from zinc dithiophosphate (ZnDTP) and a specific amount of molybdenum dithiocarbamate (MoDTC) can be used as a fuel-saving engine oil with good high-temperature deposition performance. The present invention was developed based on this knowledge.
也就是说,本发明是一种内燃机用润滑油组合物,其特征在于,其是在矿物油以及/或者合成系基础油中,调配以金属成分计为0.12质量%(质量百分比)~0.24质量%的碱土金属系清洁剂、以磷(P)成分计为0.005质量%~0.070质量%的至少含有二烷基二硫代磷酸锌(ZnDTP)的P系添加剂、以及以钼(Mo)成分计为0.030质量%~0.075质量%的二硫代氨基甲酸钼(MoDTC)而制成的,且所述P系添加剂的P成分和所述MoDTC的Mo成分满足下式(1)所表示的条件:That is to say, the present invention is a lubricating oil composition for an internal combustion engine, characterized in that it is blended in mineral oil and/or synthetic base oil in an amount of 0.12% by mass (mass percent) to 0.24% by mass in terms of metal components. % of alkaline earth metal-based cleaning agent, 0.005% to 0.070% by mass of P-based additives containing at least zinc dialkyldithiophosphate (ZnDTP) in terms of phosphorus (P) components, and in terms of molybdenum (Mo) components It is made of molybdenum dithiocarbamate (MoDTC) at 0.030% to 0.075% by mass, and the P component of the P-based additive and the Mo component of the MoDTC satisfy the conditions represented by the following formula (1):
0.5×P+Mo≤0.075 (1)0.5×P+Mo≤0.075 (1)
[式中,P表示润滑油组合物中P系添加剂的P成分的比例(质量%),Mo表示润滑油组合物中MoDTC的Mo成分的比例(质量%)]。[wherein, P represents the ratio (mass %) of the P component of the P-based additive in the lubricating oil composition, and Mo represents the ratio (mass %) of the Mo component of MoDTC in the lubricating oil composition].
本发明的内燃机用润滑油组合物优选含有以钼成分计为0.045质量%~0.075质量%的所述二硫代氨基甲酸钼。而且,本发明的内燃机用润滑油组合物优选含有以磷成分计为0.005质量%~0.050质量%的所述P系添加剂,且优选含有以金属成分计为0.15质量%~0.20质量%的所述碱土金属系清洁剂。此外,本发明的内燃机用润滑油组合物的所述基础油优选100℃时的运动粘度为3.5mm2/s~5.0mm2/s,粘度指数为110~160。The lubricating oil composition for an internal combustion engine of the present invention preferably contains the molybdenum dithiocarbamate in an amount of 0.045% by mass to 0.075% by mass as a molybdenum component. Furthermore, the lubricating oil composition for an internal combustion engine of the present invention preferably contains the P-based additive in an amount of 0.005% by mass to 0.050% by mass as a phosphorus component, and preferably contains 0.15% by mass to 0.20% by mass in terms of a metal component. Alkaline earth metal based cleaner. In addition, the base oil of the lubricating oil composition for an internal combustion engine of the present invention preferably has a kinematic viscosity at 100°C of 3.5 mm 2 /s to 5.0 mm 2 /s and a viscosity index of 110 to 160.
[发明的效果][Effect of the invention]
通过采用如上所述的构成,本发明的内燃机用润滑油组合物是可以实现下述特殊效果的长寿命节油型发动机油,即,高温沉积性能优异,即使长时间使用沉积物堆积量也较少,且可以长时间地维持低摩擦。因此,本发明的内燃机用润滑油组合物可以较好地用于内燃机,尤其是稀燃或直喷等汽油发动机或涡轮增压机,发挥出提高燃油效率的特殊效果。By adopting the above constitution, the lubricating oil composition for an internal combustion engine of the present invention is a long-life, fuel-saving engine oil capable of achieving the following special effects, that is, excellent high-temperature deposit performance and relatively low deposit accumulation even after long-term use. less, and can maintain low friction for a long time. Therefore, the lubricating oil composition for internal combustion engines of the present invention can be preferably used in internal combustion engines, especially gasoline engines or turbochargers such as lean burn or direct injection, and can exert a special effect of improving fuel efficiency.
具体实施方式 Detailed ways
本发明的内燃机用润滑油组合物的基础油可以使用矿物油、合成系基础油、以及矿物油与合成系基础油的混合物中的任意一种。该基础油在100℃时的运动粘度优选3.5mm2/s~5.0mm2/s的范围,特别优选4.0mm2/s~4.5mm2/s的范围。而且,该基础油的粘度指数优选110~160的范围,特别优选120~140的范围。另外,矿物油理想的是粘度指数大于等于120的高粘度指数润滑油基础油。粘度指数大于等于120的高粘度指数润滑油基础油可以通过下述方式而获得:对使蜡(wax)进行氢异构化或者使重质油进行氢化裂解所得的生成油进行溶剂脱蜡或氢化脱蜡。下面将对这些制造方法的一例进行具体描述。As the base oil of the lubricating oil composition for an internal combustion engine of the present invention, any of mineral oil, synthetic base oil, and a mixture of mineral oil and synthetic base oil can be used. The kinematic viscosity of the base oil at 100°C is preferably in the range of 3.5 mm 2 /s to 5.0 mm 2 /s, particularly preferably in the range of 4.0 mm 2 /s to 4.5 mm 2 /s. Furthermore, the viscosity index of the base oil is preferably in the range of 110-160, particularly preferably in the range of 120-140. In addition, the mineral oil is desirably a high viscosity index lubricating oil base oil having a viscosity index of 120 or more. A high viscosity index lubricating base oil with a viscosity index of 120 or more can be obtained by solvent dewaxing or hydrogenating the resulting oil obtained by hydroisomerizing wax or hydrocracking heavy oil Dewaxing. An example of these production methods will be specifically described below.
可以利用下述方式使蜡进行氢异构化:使用沸点为300℃~600℃的范围、碳数为20~70的范围的蜡作为原料,在氢分压为5MPa~14MPa的氢气存在下,在300℃~450℃的温度下,以0.1hr-1~2hr-1的液时空速(liquid hour space velocity,LHSV),使所述蜡和氢异构化催化剂相接触。此时,优选直链状石蜡(paraffin)的转化率大于等于80%,且直链状石蜡向轻质馏分的转化率小于等于40%。另外,原料蜡例如可以列举:在矿物油系润滑油的溶剂脱蜡步骤中获得的软蜡(slack wax)、或利用由烃气体等合成液体燃料的费托合成(Fischer-Tropsch synthesis)而获得的蜡等。而且,氢异构化催化剂例如可以列举:在氧化铝(alumina)或氧化硅(silica)-氧化铝载体上承载着镍(nickel)、钴(cobalt)等8族金属以及钼、钨(tungsten)等6A族金属中的一种或一种以上的催化剂,沸石(zeolite)催化剂或在含沸石的载体上承载着铂等的催化剂。Waxes can be hydroisomerized in the following manner: using waxes with a boiling point in the range of 300°C to 600°C and a carbon number in the range of 20 to 70 as raw materials, in the presence of hydrogen with a hydrogen partial pressure of 5MPa to 14MPa, The wax and the hydroisomerization catalyst are brought into contact at a temperature of 300° C. to 450° C. and a liquid hourly space velocity (liquid hour space velocity, LHSV) of 0.1 hr −1 to 2 hr −1 . At this time, it is preferable that the conversion rate of linear paraffin (paraffin) is not less than 80%, and the conversion rate of linear paraffin to light fraction is not more than 40%. In addition, raw material waxes include, for example, slack waxes obtained in the solvent dewaxing step of mineral oil-based lubricating oils, or those obtained by Fischer-Tropsch synthesis for synthesizing liquid fuels from hydrocarbon gases and the like. wax etc. Furthermore, examples of the hydroisomerization catalyst include those in which Group 8 metals such as nickel and cobalt, molybdenum, and tungsten are supported on an alumina or silica-alumina carrier. One or more catalysts of Group 6A metals, zeolite catalysts or catalysts containing platinum on a zeolite-containing carrier.
另一方面,可以利用下述方式进行氢化裂解:使用根据需要经过氢化脱硫及脱氮的沸点为300℃~600℃的范围的常压馏出油、减压馏出油或者光亮油(bright stock),在氢分压为7MPa~14MPa的氢气存在下,在350℃~450℃的温度下,以0.1hr-1~2hr-1的LHSV(液时空速),使所述常压馏出油、减压馏出油或者光亮油和氢化裂解催化剂相接触。此时,优选裂解率(大于等于360℃的馏分的减少量占生成物的质量百分比)为40%~90%。另外,氢化裂解催化剂例如可以列举:在氧化硅-氧化铝载体上承载着镍、钴等8族金属的一种或者一种以上以及钼、钨等6A族金属的一种或者一种以上的催化剂。On the other hand, hydrocracking can be carried out by using atmospheric distillate oil, vacuum distillate oil, or bright stock (bright stock) with a boiling point in the range of 300° C. to 600° C. that has undergone hydrodesulfurization and denitrogenation as needed. ), in the presence of hydrogen with a hydrogen partial pressure of 7MPa to 14MPa, at a temperature of 350°C to 450°C, with an LHSV (liquid hourly space velocity) of 0.1hr -1 to 2hr -1 , the atmospheric distillate oil , vacuum distillate oil or bright stock is in contact with a hydrocracking catalyst. At this time, it is preferable that the cracking rate (the reduction of the fraction greater than or equal to 360° C. in the mass percentage of the product) is 40% to 90%. In addition, examples of hydrocracking catalysts include catalysts in which one or more Group 8 metals such as nickel and cobalt and one or more Group 6A metals such as molybdenum and tungsten are supported on a silica-alumina carrier. .
从利用所述方法而获得的氢异构化生成油或者氢化裂解生成油中馏去轻质馏分后可以获得润滑油馏分,但是如果直接使用该馏分,则一般说来流动点或粘度较高,而且粘度指数并不足够高。因此,可以对该馏分进行脱蜡处理,除去蜡成分,由此获得n-d-M环分析的%Cp大于等于80,流动点小于等于-10℃,粘度指数大于等于120的润滑油基础油。The lubricating oil fraction can be obtained by distilling off the light fraction from the hydroisomerization product oil or hydrocracking product oil obtained by the above method, but if the fraction is used as it is, generally speaking, the pour point or viscosity is high, And the viscosity index is not high enough. Therefore, the fraction can be dewaxed to remove the wax components, thereby obtaining a lubricating base oil with a %C p of ndM ring analysis greater than or equal to 80, a pour point of less than or equal to -10°C, and a viscosity index of greater than or equal to 120.
在利用溶剂脱蜡处理来除去所述蜡成分的情况下,优选在馏去所述轻质馏分时,使用精密蒸馏装置进行蒸馏分离,预先进行分馏以使由气相色谱蒸馏法所得的沸点大于等于371℃而小于491℃的馏分大于等于70质量%,原因在于,由此可以更高效率地进行溶剂脱蜡处理。该溶剂脱蜡处理优选使用例如甲基乙基酮/甲苯(容量比为1/1)作为脱蜡溶剂,在溶剂和油的比为2/1~4/1的范围,温度为-15℃~-40℃的条件下进行。In the case of removing the wax component by solvent dewaxing, it is preferable to distill and separate the light fraction by using a precision distillation device, and perform fractional distillation in advance so that the boiling point obtained by the gas chromatographic distillation method is equal to or greater than The reason why the fraction of 371° C. to less than 491° C. is 70% by mass or more is that the solvent dewaxing treatment can be performed more efficiently. The solvent dewaxing treatment preferably uses, for example, methyl ethyl ketone/toluene (capacity ratio: 1/1) as the dewaxing solvent, the ratio of solvent and oil is in the range of 2/1 to 4/1, and the temperature is -15°C Carried out at ~-40°C.
另一方面,在利用氢化脱蜡法来除去所述蜡成分的情况下,下述方式的效率较高因而优选使用:以不会妨碍到氢化脱蜡的程度来馏去轻质馏分,在氢化脱蜡之后,使用精密蒸馏装置进行蒸馏分离,进行分馏以使由气相色谱蒸馏法所得的沸点大于等于371℃而小于491℃的馏分大于等于70质量%。该氢化脱蜡优选在氢分压为3MPa~15MPa的氢气存在下,在320℃~430℃的温度下,以0.2hr-1~4hr-1的LHSV(液时空速)使所述润滑油馏分与沸石催化剂相接触,以使最终润滑油基础油的流动点小于等于-10℃。On the other hand, in the case of removing the wax component by hydrodewaxing, it is preferable to use the method of distilling off light fractions to an extent that does not interfere with hydrodewaxing, and using After dewaxing, distillation separation is performed using a precision distillation apparatus, and fractional distillation is performed so that the fraction having a boiling point of not less than 371° C. and less than 491° C. obtained by gas chromatographic distillation is not less than 70% by mass. The hydrodewaxing is preferably carried out in the presence of hydrogen with a hydrogen partial pressure of 3 MPa to 15 MPa, at a temperature of 320°C to 430°C, and at an LHSV (liquid hourly space velocity) of 0.2hr -1 to 4hr -1 to make the lubricating oil fraction Contact with the zeolite catalyst so that the pour point of the final lubricating oil base oil is less than or equal to -10°C.
利用以上所述的方法,可以获得粘度指数大于等于120的润滑油基础油,并且可以根据需要进一步进行溶剂精制或者氢化精制。Using the method described above, a lubricating oil base oil with a viscosity index greater than or equal to 120 can be obtained, and further solvent refining or hydrogenation refining can be performed as required.
而且,合成系基础油可以列举:α-烯烃的低聚物,由己二酸(adipic acid)等二元酸和一元醇所合成的二酯,由新戊二醇(neopentyl glycol)、三羟甲基丙烷(trimethylolpropane)、季戊四醇(pentaerythritol)等多元醇和一元酸所合成的多元醇酯(polyol Ester),以及它们的混合物等。此外,将矿物油和合成系基础油适当组合而成的混合油也可以用作本发明的内燃机用润滑油组合物的基础油。Furthermore, examples of synthetic base oils include oligomers of α-olefins, diesters synthesized from dibasic acids such as adipic acid and monohydric alcohols, neopentyl glycol, trimethylol, etc. Trimethylolpropane (trimethylolpropane), pentaerythritol (pentaerythritol) and other polyols and polyol esters (polyol Ester) synthesized from monobasic acids, and their mixtures. In addition, a blended oil obtained by appropriately combining a mineral oil and a synthetic base oil can also be used as the base oil of the lubricating oil composition for an internal combustion engine of the present invention.
本发明的内燃机用润滑油组合物所使用的二烷基二硫代磷酸锌(ZnDTP),可以列举下述通式(2)所表示的化合物:The zinc dialkyldithiophosphate (ZnDTP) used in the lubricating oil composition for internal combustion engines of the present invention can include compounds represented by the following general formula (2):
[化1][chemical 1]
所述通式(2)中,R1、R2、R3及R4分别独立表示碳数为1~24的烃基。这些烃基是碳数为1~24的直链状或支链状烷基、碳数为3~24的直链状或支链状烯基或者直链状或支链状烷基环烷基、碳数为6~18的芳基或者直链状或支链状烷基芳基。而且,烷基或烯基可以是一级、二级以及三级中的任意一种。In the general formula (2), R 1 , R 2 , R 3 and R 4 each independently represent a hydrocarbon group having 1 to 24 carbon atoms. These hydrocarbon groups are linear or branched alkyl groups with 1 to 24 carbons, linear or branched alkenyl groups with 3 to 24 carbons, or linear or branched alkylcycloalkyl groups, An aryl group having 6 to 18 carbon atoms or a linear or branched alkylaryl group. Also, the alkyl or alkenyl may be any of primary, secondary, and tertiary.
相对于内燃机用润滑油组合物的总质量,至少含有ZnDTP的P系添加剂的含量以P系化合物所含的磷(P)元素质量计为0.005质量%~0.070质量%,优选0.005质量%~0.050质量%的范围。另外,本发明的内燃机用润滑油组合物实质上不含ZnDTP以外的P系添加剂,ZnDTP以外的P系添加剂的含量优选小于等于0.002质量%,更优选不含ZnDTP以外的P系添加剂。另外,所谓P系添加剂,是指由含有磷元素的化合物所构成的添加剂。Relative to the total mass of the lubricating oil composition for internal combustion engines, the content of the P-based additive containing at least ZnDTP is 0.005% by mass to 0.070% by mass, preferably 0.005% by mass to 0.050% by mass of the phosphorus (P) element contained in the P-based compound. mass % range. In addition, the lubricating oil composition for an internal combustion engine of the present invention does not substantially contain P-based additives other than ZnDTP, and the content of P-based additives other than ZnDTP is preferably 0.002% by mass or less, and more preferably does not contain P-based additives other than ZnDTP. In addition, the P-based additive refers to an additive composed of a compound containing phosphorus element.
本发明的内燃机用润滑油组合物所使用的二硫代氨基甲酸钼(MoDTC)可以用下述通式(3)表示:Molybdenum dithiocarbamate (MoDTC) used in the lubricating oil composition for internal combustion engines of the present invention can be represented by the following general formula (3):
[化2][Chem 2]
所述通式(3)中,R5、R6、R7及R8表示碳数为4~18的直链状或支链状烷基或者烯基,X表示氧原子或者硫原子,该氧原子和硫原子的比为1/3~3/1。R5~R8优选烷基,特别优选碳数为8~14的支链状烷基,R5~R8具体可以列举:丁基、2-乙基己基、异十三烷基、十八烷基等。另外,存在于一分子中的四个R5~R8既可以相同也可以不同。而且,本发明的内燃机用润滑油组合物中,也可以将两种或者两种以上的R5~R8不同的MoDTC混合使用。In the general formula (3), R 5 , R 6 , R 7 and R 8 represent straight-chain or branched-chain alkyl or alkenyl groups with 4 to 18 carbons, X represents an oxygen atom or a sulfur atom, and the The ratio of oxygen atoms to sulfur atoms is 1/3 to 3/1. R 5 to R 8 are preferably alkyl groups, particularly preferably branched chain alkyl groups with 8 to 14 carbon atoms. Specific examples of R 5 to R 8 include: butyl, 2-ethylhexyl, isotridecyl, octadecyl Alkyl etc. In addition, four R 5 to R 8 present in one molecule may be the same or different. Furthermore, in the lubricating oil composition for an internal combustion engine of the present invention, two or more MoDTCs having different R 5 to R 8 may be mixed and used.
相对于内燃机用润滑油组合物的总质量,MoDTC的含量以MoDTC所含的钼(Mo)元素质量计为0.030质量%~0.075质量%,优选0.045质量%~0.075质量%的范围。The content of MoDTC is in the range of 0.030% to 0.075% by mass, preferably 0.045% to 0.075% by mass, based on the mass of the molybdenum (Mo) element contained in MoDTC, relative to the total mass of the lubricating oil composition for internal combustion engines.
以下述方式来调配至少含有ZnDTP的P系化合物与MoDTC,即,使P系化合物以P成分计为0.005质量%~0.070质量%,优选0.005质量%~0.050质量%,使MoDTC以Mo成分计为0.030质量%~0.075质量%,优选0.045质量%~0.075质量%,且在0.5×P+Mo≤0.075的范围内。如果0.5×P+Mo的值大于0.075,则不能获得目标的高温沉积性能,例如,TEOST 33C试验的沉积物质量不会小于等于42mg。而且,如果所述P系化合物的含量以P成分计小于0.005质量%,则不能获得目标的耐磨耗性能,如果所述P系化合物的含量以P成分计大于0.070质量%,则对使尾气净化催化剂中毒的影响变大。另一方面,如果所述MoDTC的含量以Mo成分计小于0.030质量%,则不能获得目标的节油性能,如果所述MoDTC的含量以Mo成分计大于0.075质量%,则不能获得目标的高温沉积性能。另外,如果MoDTC的含量以Mo成分计大于等于0.045质量%,则可以获得节油性能的高持续性。The P-based compound containing at least ZnDTP and MoDTC are prepared in such a manner that the P-based compound is 0.005 mass % to 0.070 mass % as the P component, preferably 0.005 mass % to 0.050 mass %, and the MoDTC is calculated as the Mo component. 0.030% by mass to 0.075% by mass, preferably 0.045% by mass to 0.075% by mass, and within the range of 0.5×P+Mo≦0.075. If the value of 0.5×P+Mo is greater than 0.075, the target high-temperature deposition performance cannot be obtained, for example, the deposit mass of the TEOST 33C test will not be less than or equal to 42 mg. Moreover, if the content of the P-based compound is less than 0.005% by mass in terms of the P component, the target wear resistance cannot be obtained, and if the content of the P-based compound is greater than 0.070% by mass in terms of the P component, it is harmful to exhaust gas. The influence of purification catalyst poisoning becomes greater. On the other hand, if the content of the MoDTC is less than 0.030% by mass based on the Mo component, the targeted fuel-saving performance cannot be obtained, and if the content of the MoDTC is greater than 0.075% by mass based on the Mo component, the targeted high-temperature deposition cannot be obtained. performance. In addition, if the content of MoDTC is equal to or greater than 0.045% by mass based on the Mo component, high sustainability of fuel-saving performance can be obtained.
从清洁性的观点来说,本发明的内燃机用润滑油组合物优选含有碱土金属系清洁剂。该金属系清洁剂优选使用选自碱土金属磺酸盐、碱土金属酚盐以及碱土金属水杨酸盐中的至少一种碱土金属清洁剂。From the viewpoint of detergency, the lubricating oil composition for an internal combustion engine of the present invention preferably contains an alkaline earth metal-based detergent. The metal-based detergent is preferably at least one alkaline earth metal detergent selected from alkaline earth metal sulfonates, alkaline earth metal phenates, and alkaline earth metal salicylates.
所述碱土金属磺酸盐可以使用分子量优选为300~1,500、特别优选为400~700的烷基芳香族磺酸的碱土金属盐,优选使用镁盐以及/或者钙盐,特别优选使用钙盐。The alkaline earth metal sulfonate may be an alkaline earth metal salt of an alkylaromatic sulfonic acid with a molecular weight of preferably 300-1,500, particularly preferably 400-700, preferably a magnesium salt and/or a calcium salt, particularly preferably a calcium salt.
所述碱土金属酚盐可以列举烷基酚(alkyl phenol)、烷基酚硫化物(alkyl phenolsulfide)、烷基酚的曼尼希(Mannich)反应物的碱土金属盐,特别是镁盐以及/或者钙盐,更具体来说,可以列举下述通式(4)~通式(6)所表示的化合物:Described alkaline earth metal phenate can enumerate the alkaline earth metal salt of alkylphenol (alkylphenol), alkylphenolsulfide (alkylphenolsulfide), the Mannich (Mannich) reactant of alkylphenol, particularly magnesium salt and/or Calcium salts, more specifically, compounds represented by the following general formulas (4) to (6):
[化3][Chem 3]
[化4][chemical 4]
[化5][chemical 5]
所述通式(4)~通式(6)中,R9、R10、R11、R12、R13及R14分别独立表示碳数为4~30、优选为6~18的直链状或支链状烷基,M1、M2及M3分别表示碱土金属,优选为钙以及/或者镁,x表示1或者2。In the general formulas (4) to (6), R 9 , R 10 , R 11 , R 12 , R 13 and R 14 each independently represent a straight chain with 4 to 30 carbon atoms, preferably 6 to 18 carbon atoms. Shaped or branched chain alkyl, M 1 , M 2 and M 3 represent alkaline earth metals, preferably calcium and/or magnesium, and x represents 1 or 2.
所述碱土金属水杨酸盐可以列举烷基水杨酸的碱土金属盐,特别优选镁盐以及/或者钙盐,更具体来说,可以列举下述通式(7)所表示的化合物:The alkaline earth metal salicylate can be an alkaline earth metal salt of alkyl salicylic acid, particularly preferably a magnesium salt and/or a calcium salt, more specifically, a compound represented by the following general formula (7):
[化6][chemical 6]
所述通式(7)中,R15分别独立表示碳数为1~30、优选为6~18的直链状或支链状烷基,n表示1~4的整数,优选1或者2,M4表示碱土金属,优选钙以及/或者镁。In the general formula (7), R 15 each independently represent a linear or branched alkyl group with a carbon number of 1 to 30, preferably 6 to 18, n represents an integer of 1 to 4, preferably 1 or 2, M 4 represents an alkaline earth metal, preferably calcium and/or magnesium.
本发明的内燃机用润滑油组合物中的金属系清净剂的含量优选为,相对于内燃机用润滑油组合物的总质量,以金属成分计为0.12质量%~0.24质量%的范围,更优选0.15质量%~0.20质量%的范围。如果所述金属系清洁剂的含量以金属成分计小于0.12质量%,则不能获得目标的清洁性,如果所述金属系清洁剂的含量以金属成分计大于0.24质量%,则灰分可能会堆积在燃烧室内,因而不佳。The content of the metal-based detergent in the lubricating oil composition for internal combustion engines of the present invention is preferably in the range of 0.12% by mass to 0.24% by mass in terms of metal components, more preferably 0.15% by mass, based on the total mass of the lubricating oil composition for internal combustion engines. The range of mass % - 0.20 mass %. If the content of the metal-based detergent is less than 0.12% by mass in terms of metal components, the targeted cleaning performance cannot be obtained, and if the content of the metal-based detergent is greater than 0.24% by mass in terms of metal components, ash may be deposited in the In the combustion chamber, it is not good.
而且,从清洁性以及油泥(sludge)分散性的观点来说,本发明的内燃机用润滑油组合物优选含有无灰分散剂。无灰分散剂可以列举由聚烯烃衍生所得的烯基琥珀酰亚胺,烷基琥珀酰亚胺以及它们的衍生物。具代表性的琥珀酰亚胺可以通过使被高分子量的烯基或者烷基置换的琥珀酸酐、与每一分子中平均含有4个~10个(优选5个~7个)氮原子的聚亚烷基多胺(polyalkylene polyamine)反应而获得。高分子量的烯基或者烷基优选数量平均分子量为700~5000的聚异丁烯基,特别优选数量平均分子量为900~3000的聚异丁烯基。Furthermore, the lubricating oil composition for an internal combustion engine of the present invention preferably contains an ashless dispersant from the viewpoint of detergency and sludge dispersibility. Examples of ashless dispersants include alkenyl succinimide, alkyl succinimide and their derivatives derived from polyolefin. A representative succinimide can be obtained by making succinic anhydride substituted by a high molecular weight alkenyl or alkyl group, and polyamethylene oxide containing an average of 4 to 10 (preferably 5 to 7) nitrogen atoms in each molecule. It is obtained by reaction of polyalkylene polyamine. The high-molecular-weight alkenyl or alkyl group is preferably a polyisobutenyl group with a number average molecular weight of 700 to 5,000, particularly preferably a polyisobutenyl group with a number average molecular weight of 900 to 3,000.
本发明的内燃机用润滑油组合物所使用的聚丁烯基琥珀酰亚胺可以列举下述通式(8)或者通式(9)表示的化合物:The polybutenyl succinimide used in the lubricating oil composition for internal combustion engines of the present invention can include compounds represented by the following general formula (8) or general formula (9):
[化7][chemical 7]
[化8][chemical 8]
所述通式(8)以及通式(9)中,PIB表示聚丁烯基,是利用下述聚丁烯所得的基团,即,此聚丁烯是使用氟化硼系催化剂或氯化铝系催化剂,使高纯度异丁烯或1-丁烯和异丁烯的混合物进行聚合而获得的,并且,所述聚丁烯基中通常含有5mol%~100mol%的在聚丁烯末端具有亚乙烯(vinylidene)基结构的基团。另外,从油泥抑制效果优异的观点来说,n优选2~5的整数,特别优选3~4的整数。In the general formula (8) and general formula (9), PIB represents a polybutenyl group, which is a group obtained by using the following polybutene, that is, this polybutene is obtained by using a boron fluoride-based catalyst or chlorinated Aluminum-based catalysts are obtained by polymerizing high-purity isobutene or a mixture of 1-butene and isobutene, and the polybutene group usually contains 5 mol% to 100 mol% of vinylidene (vinylidene) at the end of the polybutene ) group of the base structure. In addition, n is preferably an integer of 2 to 5, particularly preferably an integer of 3 to 4, from the viewpoint of an excellent sludge inhibiting effect.
而且,聚丁烯基琥珀酰亚胺的衍生物可以使用所谓的改性琥珀酰亚胺,即,使所述式(8)或者式(9)表示的化合物,与硼酸等硼化合物或醇、醛、酮、烷基酚、环状碳酸酯、有机酸等含氧有机化合物作用,并将残留的氨基以及/或者亚氨基的一部分或全部中和或者使它们形成酰氨基。尤其是,使所述式(8)或者式(9)表示的化合物与硼酸等硼化合物反应而获得的含硼的烯基(或烷基)琥珀酰亚胺在热稳定性、氧化稳定性方面较为有利。Furthermore, as a derivative of polybutenyl succinimide, a so-called modified succinimide can be used, that is, a compound represented by the above-mentioned formula (8) or formula (9), and a boron compound such as boric acid or alcohol, Aldehydes, ketones, alkylphenols, cyclic carbonates, organic acids and other oxygen-containing organic compounds, and neutralize part or all of the remaining amino groups and/or imino groups or make them form amido groups. In particular, the boron-containing alkenyl (or alkyl) succinimide obtained by reacting the compound represented by the formula (8) or the formula (9) with a boron compound such as boric acid has the advantages of thermal stability and oxidation stability. more favorable.
本发明的内燃机用润滑油组合物中的无灰分散剂的含量为任意含量,优选相对于内燃机用润滑油组合物的总质量为0.5质量%~15质量%的范围。The content of the ashless dispersant in the lubricating oil composition for internal combustion engines of the present invention is arbitrary, and is preferably in the range of 0.5% by mass to 15% by mass relative to the total mass of the lubricating oil composition for internal combustion engines.
本发明的内燃机用润滑油组合物中,除了所述ZnDTP、MoDTC、金属系清洁剂以及无灰分散剂之外,可以根据需要添加无灰系抗氧化剂、粘度指数改进剂、流动点下降剂、金属钝化剂、防锈剂或消泡剂等添加剂。In the lubricating oil composition for internal combustion engines of the present invention, in addition to the ZnDTP, MoDTC, metal-based detergents and ashless dispersants, ashless antioxidants, viscosity index improvers, pour point depressants, metal Additives such as passivators, rust inhibitors or defoamers.
[实施例][Example]
下面,列举实施例来更详细地说明本发明,但本发明不受下述实施例的任何限定。Hereinafter, examples are given to illustrate the present invention in more detail, but the present invention is not limited at all by the following examples.
使用对使重质油进行氢化裂解所得的生成油进行氢化脱蜡而获得的矿物油系基础油[运动粘度:19.9mm2/s(40℃)、4.26mm2/s(100℃);粘度指数为121],来作为基础油。Mineral oil-based base oil obtained by hydrodewaxing the product oil obtained by hydrocracking heavy oil [kinematic viscosity: 19.9 mm 2 /s (40°C), 4.26 mm 2 /s (100°C); viscosity The index is 121], as the base oil.
以表1所示的比例,在所述基础油中调配MoDTC、ZnDTP以及其他添加剂,制备实施例1~实施例2以及比较例1~比较例5的内燃机用润滑油组合物(发动机油)。并且,将0.5×P+Mo的值一起示于表1中。另外,碱土金属系清洁剂是使用磺酸钙,ZnDTP是使用以所述通式(2)表示的R1、R2、R3及R4为辛基的化合物,以及R1、R2、R3及R4为丁基及戊基的化合物,MoDTC是使用以所述通式(3)表示的R5、R6、R7及R8为2-乙基己基,且X的氧原子与硫原子的比(O/S)为1/1的化合物。另外,其他添加剂是包含烯基琥珀酰亚胺、粘度指数改进剂、流动点下降剂以及消泡剂的添加剂混合物,在所有实施例以及比较例中均添加相同量的添加剂。MoDTC, ZnDTP and other additives were blended in the base oil at the ratio shown in Table 1 to prepare lubricating oil compositions (engine oils) for internal combustion engines of Examples 1-2 and Comparative Examples 1-5. In addition, the values of 0.5×P+Mo are shown in Table 1 together. In addition, the alkaline earth metal-based detergent uses calcium sulfonate, ZnDTP uses a compound in which R 1 , R 2 , R 3 and R 4 represented by the general formula (2) are octyl groups, and R 1 , R 2 , R 3 and R 4 are butyl and pentyl compounds, and MoDTC uses R 5 , R 6 , R 7 and R 8 represented by the general formula (3) as 2-ethylhexyl, and the oxygen atom of X A compound with a sulfur atom ratio (O/S) of 1/1. In addition, other additives are additive mixtures containing alkenyl succinimide, a viscosity index improver, a pour point depressant, and an antifoaming agent, and the same amount of additives was added in all Examples and Comparative Examples.
[表1][Table 1]
对表1的实施例以及比较例的发动机油分别实施TEOST 33C试验,评价发动机油的性能。TEOST 33C试验是利用沉积物质量来评价高温沉积性能的项目,在作为发动机油标准的ILSAC GF-2标准中,规定将沉积物质量小于等于60mg作为合格标准。依据ASTM D6335来求出所述各供试发动机油的沉积物质量。而且,利用SHELL四球磨耗试验来评价供试发动机油的耐磨耗性能,耐磨耗性能良好时记作○,不良时记作×。此外,利用SRV摩擦试验来评价供试发动机油的节油性,节油性特别好时记作◎,良好时记作○,不良时记作×。将这些结果示于表2中。The TEOST 33C test was performed on the engine oils of Examples and Comparative Examples in Table 1, respectively, to evaluate the performance of the engine oils. The TEOST 33C test is a project that uses the quality of sediment to evaluate the high-temperature deposition performance. In the ILSAC GF-2 standard, which is the engine oil standard, it is stipulated that the quality of sediment should be less than or equal to 60mg as the qualified standard. According to ASTM D6335, the deposit quality of each of the test engine oils was obtained. Furthermore, the wear resistance of the engine oil to be tested was evaluated by the SHELL four-ball abrasion test, and when the wear resistance was good, it was marked as ○, and when it was bad, it was marked as ×. In addition, the SRV friction test was used to evaluate the fuel-saving performance of the test engine oil, and the fuel-saving performance was marked as ◎, good as ○, and poor as x. These results are shown in Table 2.
[表2][Table 2]
以上结果表明,实施例所示的在矿物油以及/或者合成系基础油中,调配以P成分计为0.005质量%~0.070质量%的至少含有ZnDTP的P系化合物、以及以Mo成分计为0.030质量%~0.075质量%的MoDTC而制成的,且将0.5×P+Mo调整为小于等于0.075的内燃机用润滑油组合物在TEOST 33C试验中的沉积物质量,比ILSAC GF-2标准所规定的小于等于60mg进一步减少了三成或三成以上,可见此内燃机用润滑油组合物的高温沉积性能良好。此外可知,由于高浓度地调配有MoDTC,因此节油性优异。The above results show that in the mineral oil and/or synthetic base oil shown in the examples, a P-based compound containing at least ZnDTP in an amount of 0.005 mass % to 0.070 mass % in terms of a P component, and 0.030 mass % in terms of a Mo component are blended. mass % to 0.075 mass % MoDTC, and adjust 0.5×P+Mo to be less than or equal to 0.075, the deposit quality of the lubricating oil composition for internal combustion engines in the TEOST 33C test is higher than that stipulated in the ILSAC GF-2 standard 30% or more is further reduced by 30% or more, which shows that the high-temperature deposition performance of the lubricating oil composition for internal combustion engines is good. In addition, it can be seen that since MoDTC is formulated at a high concentration, it is excellent in fuel economy.
另一方面可知,0.5×P+Mo的值大于0.075的比较例2以及比较例3中,沉积物质量较大,高温沉积性能差。另外,没有调配MoDTC的比较例4虽然0.5×P+Mo的值较小,高温沉积性能优异,但节油性差。此外,没有调配ZnDTP的比较例5虽然0.5×P+Mo的值较小,高温沉积性能优异,但耐磨耗性能差。On the other hand, it can be seen that in Comparative Example 2 and Comparative Example 3 where the value of 0.5×P+Mo is greater than 0.075, the quality of the deposit is large and the high-temperature deposition performance is poor. In addition, in Comparative Example 4 without MoDTC, although the value of 0.5×P+Mo is small and the high-temperature deposition performance is excellent, the fuel-saving performance is poor. In addition, although the value of 0.5×P+Mo is small in Comparative Example 5 without ZnDTP, the high-temperature deposition performance is excellent, but the abrasion resistance performance is poor.
以上所述,仅是本发明的较佳实施例而已,并非对本发明作任何形式上的限制,虽然本发明已以较佳实施例揭露如上,然而并非用以限定本发明,任何熟悉本专业的技术人员,在不脱离本发明技术方案范围内,当可利用上述揭示的技术内容作出些许更动或修饰为等同变化的等效实施例,但凡是未脱离本发明技术方案的内容,依据本发明的技术实质对以上实施例所作的任何简单修改、等同变化与修饰,均仍属于本发明技术方案的范围内。The above description is only a preferred embodiment of the present invention, and does not limit the present invention in any form. Although the present invention has been disclosed as above with preferred embodiments, it is not intended to limit the present invention. Anyone familiar with this field Those skilled in the art, without departing from the scope of the technical solution of the present invention, can use the technical content disclosed above to make some changes or modify equivalent embodiments with equivalent changes, but all the content that does not depart from the technical solution of the present invention, according to the present invention Any simple modifications, equivalent changes and modifications made to the above embodiments by the technical essence still belong to the scope of the technical solution of the present invention.
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