LUBRICANT COMPOSITION FOR HYDRAULIC OIL

Abstract
The present invention relates to a lubricant composition, and more particularly to a lubricant composition, which has superior oxidation stability and friction characteristics even under harsh conditions of high temperature and high pressure and is thus suitable for use in hydraulic oil. The lubricant composition of the present invention includes a base oil, a liquid olefin copolymer, a phosphorothioate compound, and phosphonium phosphate.
Description
CROSS-REFERENCE TO RELATED APPLICATIONS

This application is based on and claims priority from Korean Patent Application No. 10-2019-0023681, filed on Feb. 28, 2019 with the Korean Intellectual Property Office, the disclosure of which is incorporated herein in its entirety by reference.


BACKGROUND OF THE INVENTION
1. Technical Field

The present invention relates to a lubricant composition, and more particularly to a lubricant composition, which has superior oxidation stability and friction characteristics even under harsh conditions of high temperature and high pressure and is thus suitable for use in hydraulic oil.


2. Description of the Related Art

A lubricant is an oily material used to reduce the generation of frictional force on the friction surface of a machine or to dissipate frictional heat generated from the friction surface. Because of the wide variety of machinery that requires lubrication and the wide variety of conditions under which such machinery works, lubricants vary in type and quality. Depending on the application thereof, different types of base oil must be used. In particular, when a lubricant is used for an airplane or an advanced hydraulic system, hydraulic oil having a strong flame-retarding effect is required.


Any type of hydraulic oil used in industrial fields is a medium of power transmission and plays roles in lubrication, rust prevention, sealing and cooling of respective parts of hydraulic equipment. The hydraulic oil is manufactured by adding additives to base oil, and is largely classified into mineral hydraulic oil (petroleum-based hydraulic oil) and synthetic hydraulic oil depending on the type of base oil, synthetic hydraulic oil being classified into polyalphaolefin-based hydraulic oil and ester-based hydraulic oil.


Meanwhile, the operating temperature range of hydraulic oil varies, and especially in the summer, may be 75 to 850 or higher. At such temperatures, however, mineral hydraulic oil and polyalphaolefin-based hydraulic oil generate a lot of oil vapor. The occurrence of such oil vapor causes a problem of increasing the evaporation loss of hydraulic oil, and also promotes the oxidation of hydraulic oil. Hence, it is necessary to minimize the generation of oil vapor. In particular, mineral hydraulic oil, which accounts for most hydraulic oil, requires additional measures to improve oxidation stability due to the characteristics of the base feedstock oil. Moreover, since hydraulic systems are recently becoming more and more sophisticated, hydraulic oil is required to have superior friction characteristics.


Therefore, the present inventors have developed a lubricant composition for hydraulic oil, which has superior thermal and oxidation stability and is capable of reducing mechanical wear of hydraulic equipment.


CITATION LIST
Patent Literature

(Patent Document 0001) Korean Patent No. 10-0201759


(Patent Document 0002) Korean Patent Application Publication No. 10-2008-0109015


SUMMARY OF THE INVENTION

Accordingly, the present invention has been made keeping in mind the problems encountered in the related art, and an objective of the present invention is to provide a lubricant composition, in which a functional additive for friction reduction and an ethylene-alphaolefin liquid random copolymer having a high viscosity index are mixed, thereby exhibiting superior friction characteristics, thermal stability and oxidation stability.


Another objective of the present invention is to provide a lubricant composition for hydraulic oil, which is capable of reducing the mechanical wear of hydraulic equipment and energy consumption when applied to hydraulic equipment and of decreasing evaporation loss due to low changes in the physical properties of hydraulic oil, and thus may be used for a long period of time.


In order to accomplish the above objectives, the present invention provides a lubricant composition, comprising a base oil, a liquid olefin copolymer, a phosphorothioate compound, and phosphonium phosphate.


The base oil may be at least one selected from the group consisting of mineral oil, polyalphaolefin (PAO) and ester.


The liquid olefin copolymer may be prepared by copolymerizing ethylene and alphaolefin in the presence of a single-site catalyst system, and the single-site catalyst system preferably includes a metallocene catalyst, an organometallic compound and an ionic compound.


The liquid olefin copolymer may have a coefficient of thermal expansion of 3.0 to 4.0.


The liquid olefin copolymer may be included in an amount of 0.5 to 30 wt %, and preferably 0.5 to 25 wt %, in the lubricant composition of the present invention.


The phosphorothioate compound may be included in an amount of 0.1 to 5.0 wt %, and preferably 0.1 to 3.0 wt %, in the lubricant composition.


The phosphonium phosphate may be included in an amount of 0.05 to 3.0 wt %, and preferably 0.1 to 1.5 wt %, in the lubricant composition.


The lubricant composition may have an SRV friction coefficient of 0.1 to 0.35 and a traction coefficient of 0.15 to 0.3.


According to the present invention, a lubricant composition includes phosphorothioate, phosphonium phosphate, and an ethylene-alphaolefin liquid random copolymer having a high viscosity index, which are mixed together, thereby improving friction characteristics and thermal and oxidation stability, and is capable of reducing the mechanical wear of hydraulic equipment and energy consumption when applied to hydraulic equipment, thereby maximizing energy-saving effects.


Also, according to the present invention, the lubricant composition has low changes in the physical properties of hydraulic oil, thus decreasing evaporation loss, and can endure 1000 min or more, and preferably 1200 min or more, in an RBOT oxidation stability test (ASTM D2271), thereby enabling the long-term use thereof as hydraulic oil.







DESCRIPTION OF SPECIFIC EMBODIMENTS

Hereinafter, a detailed description will be given of the present invention.


The present invention relates to a lubricant composition, which has superior oxidation stability and friction characteristics and is thus suitable for use in hydraulic oil. Hence, the lubricant composition of the present invention includes a base oil, a liquid olefin copolymer, a phosphorothioate compound, and phosphonium phosphate.


Here, the base oil varies from the aspects of viscosity, heat resistance, oxidation stability and the like depending on the manufacturing method or refining method, but is generally classified into mineral oil and synthetic oil. The API (American Petroleum Institute) classifies base oil into five types, namely Group I, II, III, IV and V. These types, based on API ranges, are defined in API Publication 1509, 15th Edition, Appendix E, April 2002, and are shown in Table 1 below.













TABLE 1







Saturated





hydrocarbon (%)
Sulfur (%)
Viscosity index





















Group I
<90
>0.03
80 ≤ VI < 120



Group II
≥90
≤0.03
80 ≤ VI < 120



Group III
≥90
≤0.03
VI ≥ 120










Group IV
PAO (Poly Alpha Olefin)



Group V
Ester & Others










In the lubricant composition of the present invention, the base oil may be at least one selected from the group consisting of mineral oil, polyalphaolefin (PAO) and ester, and may be any type among Groups I to V based on the API ranges.


More specifically, mineral oil belongs to Groups I to III based on the API ranges, and mineral oil may include oil resulting from subjecting a lubricant distillate fraction, obtained through atmospheric distillation and/or vacuum distillation of crude oil, to at least one refining process of solvent deasphalting, solvent extraction, hydrogenolysis, solvent dewaxing, catalytic dewaxing, hydrorefining, sulfuric acid cleaning, and white clay treatment; wax isomerized mineral oil; or a gas-to-liquid (GLT) oil obtained via the Fischer-Tropsch process.


The synthetic oil belongs to Group IV or V based on the API ranges, and polyalphaolefin belonging to Group IV may be obtained through oligomerization of a higher alphaolefin using an acid catalyst, as disclosed in U.S. Pat. Nos. 3,780,128, 4,032,591, Japanese Patent Application Publication No. Hei. 1-163136, and the like, but the present invention is not limited thereto.


Examples of the synthetic oil belonging to Group V include alkyl benzenes, alkyl naphthalenes, isobutene oligomers or hydrides thereof, paraffins, polyoxy alkylene glycol, dialkyl diphenyl ether, polyphenyl ether, ester, and the like.


Here, the alkyl benzenes and alkyl naphthalenes are usually dialkylbenzene or dialkylnaphthalene having an alkyl chain length of 6 to 14 carbon atoms, and the alkyl benzenes or alkyl naphthalenes are prepared through Friedel-Crafts alkylation of benzene or naphthalene with olefin. The alkylated olefin used in the preparation of alkyl benzenes or alkyl naphthalenes may be linear or branched olefins or combinations thereof.


Also, examples of the ester include, but are not limited to, ditridecyl glutarate, di-2-ethylhexyl adipate, diisodecyl adipate, ditridecyl adipate, di-2-ethylhexyl sebacate, tridecyl pelargonate, di-2-ethylhexyl adipate, di-2-ethylhexyl azelate, trimethylolpropane caprylate, trimethylolpropane pelargonate, trimethylolpropane triheptanoate, pentaerythritol 2-ethylhexanoate, pentaerythritol pelargonate, pentaerythritol tetraheptanoate, and the like.


In the lubricant composition of the present invention, the liquid olefin copolymer is prepared by copolymerizing ethylene and alphaolefin monomers in the presence of a single-site catalyst system in order to uniformly distribute alphaolefin units in the copolymer chain. Preferably, the liquid olefin copolymer is prepared by reacting ethylene and alphaolefin monomers in the presence of a single-site catalyst system including a crosslinked metallocene compound, an organometallic compound, and an ionic compound for forming an ion pair through reaction with the crosslinked metallocene compound.


Here, the metallocene compound included in the single-site catalyst system may be at least one selected from the group consisting of Chemical Formulas 1 to 6 below.




embedded image


In Chemical Formulas 1 to 4,


M is a transition metal selected from the group consisting of titanium, zirconium, and hafnium,


B is absent or is a linking group including a C1-C20 alkylene group, a C6-C20 arylene group, C1-C20 dialkyl silicon, C1-C20 dialkyl germanium, a C1-C20 alkylphosphine group or a C1-C20 alkylamine group,


X1 and X2, which are the same as or different from each other, are each independently a halogen atom, a C1-C20 alkyl group, a C2-C20 alkenyl group, a C2-C20 alkynyl group, a C6-C20 aryl group, a C7-C40 alkylaryl group, a C7-C40 arylalkyl group, a C1-C20 alkylamido group, a C6-C20 arylamido group, a C1-C20 alkylidene group or a C1-C20 alkoxy group, and


R1 to R10, which are the same as or different from each other, are each independently hydrogen, a C1-C20 alkyl group, a C2-C20 alkenyl group, a C6-C20 aryl group, a C7-C20 alkylaryl group, a C7-C20 arylalkyl group, a C5-C60 cycloalkyl group, a C4-C20 heterocyclic group, a C1-C20 alkynyl group, a C6-C20-aryl-containing hetero group or a silyl group.




embedded image


In Chemical Formulas 5 and 6,


M is a transition metal selected from the group consisting of titanium, zirconium, and hafnium,


B is absent or is a linking group including a C1-C20 alkylene group, a C6-C20 arylene group, a C1-C20 dialkyl silicon, a C1-C20 dialkyl germanium, a C1-C20 alkylphosphine group or a C1-C20 alkylamine group,


X1 and X2, which are the same as or different from each other, are each independently a halogen atom, a C1-C20 alkyl group, a C2-C20 alkenyl group, a C2-C20 alkynyl group, a C6-C20 aryl group, a C7-C40 alkylaryl group, a C7-C40 arylalkyl group, a C1-C20 alkylamido group, a C6-C20 arylamido group, a C1-C20 alkylidene group or a C1-C20 alkoxy group, and


R1 to R10, which are the same as or different from each other, are each independently hydrogen, a C1-C20 alkyl group, a C2-C20 alkenyl group, a C6-C20 aryl group, a C7-C20 alkylaryl group, a C7-C20 arylalkyl group, a C5-C60 cycloalkyl group, a C4-C20 heterocyclic group, a C1-C20 alkynyl group, a C6-C20-aryl-containing hetero group or a silyl group.


Furthermore, all of R11, R13 and R14 are hydrogen, and each of R12 radicals, which are the same as or different from each other, may independently be hydrogen, a C1-C20 alkyl group, a C2-C20 alkenyl group, a C6-C20 aryl group, a C7-C20 alkylaryl group, a C7-C20 arylalkyl group, a C5-C60 cycloalkyl group, a C4-C20 heterocyclic group, a C1-C20 alkynyl group, a C6-C20-aryl-containing hetero group or a silyl group.


Also, the metallocene compound of Chemical Formulas 2 to 6 may include a compound substituted through a hydroaddition reaction, and a preferred example thereof includes dimethylsilyl bis(tetrahydroindenyl) zirconium dichloride.


The organometallic compound included in the single-site catalyst system may be at least one selected from the group consisting of an organoaluminum compound, an organomagnesium compound, an organozinc compound and an organolithium compound, and is preferably an organoaluminum compound. The organoaluminum compound may be at least one selected from the group consisting of, for example, trimethylaluminum, triethylaluminum, triisobutylaluminum, tripropylaluminum, tributylaluminum, dimethylchloroaluminum, dimethylisobutylaluminum, dimethylethylaluminum, diethylchloroaluminum, triisopropylaluminum, triisobutylaluminum, tricyclopentylaluminum, tripentylaluminum, triisopentylaluminum, ethyldimethylaluminum, methyldiethylaluminum, triphenylaluminum, methylaluminoxane, ethylaluminoxane, isobutylaluminoxane and butylaluminoxane, and is preferably triisobutylaluminum.


The ionic compound included in the single-site catalyst system may be at least one selected from the group consisting of organoboron compounds such as dimethylanilinium tetrakis(perfluorophenyl)borate, triphenylcarbenium tetrakis(perfluorophenyl)borate, and the like.


The component ratio of the single-site catalyst system may be determined in consideration of catalytic activity, and the molar ratio of metallocene catalyst:ionic compound:organometallic compound is preferably adjusted in the range of 1:1:5 to 1:10:1000 in order to ensure desired catalytic activity.


Furthermore, the components of the single-site catalyst system may be added at the same time or in any sequence to an appropriate solvent and may thus function as an active catalyst system. Here, the solvent may include, but is not limited to, a hydrocarbon solvent such as pentane, hexane, heptane, etc., or an aromatic solvent such as benzene, toluene, xylene, etc., and any solvent usable in the preparation may be used.


Also, the alphaolefin monomer used in the preparation of the liquid olefin copolymer includes a C2-C20 aliphatic olefin, and may specifically be at least one selected from the group consisting of ethylene, propylene, 1-butene, 1-pentene, 3-methyl-1-butene, 1-hexene, 4-methyl-1-pentene, 3-methyl-1-pentene, 1-heptene, 1-octene, 1-decene, 1-dodecene and 1-tetradecene, and may include isomeric forms, but the present invention is not limited thereto. In the copolymerization, the monomer content is 1 to 95 mol %, preferably 5 to 90 mol %.


The liquid olefin copolymer required in the present invention has a coefficient of thermal expansion of 3.0 to 4.0 and a bromine number of 0.1 or less.


The liquid olefin copolymer may be included in an amount of 0.5 to 30 wt %, and preferably 0.5 to 25 wt %, based on 100 wt % of the lubricant composition. If the amount of the liquid olefin copolymer is less than 0.5 wt % based on 100 wt % of the lubricant composition, stability may deteriorate. On the other hand, if the amount thereof exceeds 30 wt %, application of the resulting composition to hydraulic oil becomes difficult, which is undesirable.


The phosphorothioate compound, serving as a friction-reducing agent, may be at least one selected from the group consisting of monophosphorothioate, diphosphorothioate, triphosphorothioate, methylphosphorothioate, ethylphosphorothioate and sulfonylphosphorothioate. When the phosphorothioate compound is included in the lubricant composition, it may exhibit synergistic effects with an existing wear-resistant agent and friction reduction effects, and additionally, energy-saving effects may be achieved through friction reduction.


The phosphorothioate compound may be included in an amount of 0.1 to 5.0 wt %, and preferably 0.1 to 3.0 wt %, based on 100 wt % of the lubricant composition. If the amount of the phosphorothioate compound is less than 0.1 wt % based on 100 wt % of the lubricant composition, the friction reduction effect is insignificant. On the other hand, if the amount thereof exceeds 5.0 wt %, the additional reduction effect is insignificant despite the excessive addition thereof, which is undesirable.


The phosphonium phosphate is a material having the structure of Chemical Formula 7 below, and is used as a friction/wear-reducing agent. In particular, when it is used together with the phosphorothioate compound, the effects thereof may be maximized.




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The phosphonium phosphate exists in the form of an ionic liquid having both a phosphonium anion and a phosphate cation, and, among various phosphonium compounds, exhibits a characteristic friction/wear reduction effect.


Also, the phosphonium phosphate may be included in an amount of 0.05 to 3.0 wt %, and preferably 0.1 to 1.5 wt %, based on 100 wt % of the lubricant composition. If the amount of the phosphonium phosphate is less than 0.05 wt % based on 100 wt % of the lubricant composition, the friction/wear reduction effect may be insignificant. On the other hand, if the amount thereof exceeds 3.0 wt %, there is no synergistic effect thereof with the phosphorothioate compound, and wear may increase, which is undesirable.


The lubricant composition of the present invention may further include an additive selected from the group consisting of an antioxidant, a metal cleaner, an anticorrosive agent, a foam inhibitor, a pour-point depressant, a viscosity modifier, a wear-resistant agent and combinations thereof.


The antioxidant may be included in an amount of 0.01 to 5.0 wt % based on 100 wt % of the lubricant composition, and is preferably used in the form of a mixture of a phenolic antioxidant and an aminic antioxidant, more preferably a mixture of 0.01 to 3.0 wt % of the phenolic antioxidant and 0.01 to 3.0 wt % of the aminic antioxidant.


The phenolic antioxidant may be any one selected from the group consisting of 2,6-dibutylphenol, hindered bisphenol, high-molecular-weight hindered phenol, and hindered phenol with thioether.


The aminic antioxidant may be any one selected from the group consisting of diphenylamine, alkylated diphenylamine and naphthylamine, and preferably, the alkylated diphenylamine is dioctyldiphenylamine, octylated diphenylamine, or butylated diphenylamine.


The metal cleaner may be at least one selected from the group consisting of metallic phenate, metallic sulfonate, and metallic salicylate, and preferably, the metal cleaner is included in an amount of 0.1 to 10.0 wt % based on 100 wt % of the lubricant composition.


The anticorrosive agent may be a benzotriazole derivative, and is preferably any one selected from the group consisting of benzotriazole, 2-methylbenzotriazole, 2-phenylbenzotriazole, 2-ethylbenzotriazole and 2-propylbenzotriazole. The anticorrosive agent may be included in an amount of 0 to 4.0 wt % based on 100 wt % of the lubricant composition.


The foam inhibitor may be polyoxyalkylene polyol, and preferably, the foam inhibitor is included in an amount of 0 to 4.0 wt % based on 100 wt % of the lubricant composition.


The pour-point depressant may be poly(methacrylate), and preferably, the pour-point depressant is included in an amount of 0.01 to 5.0 wt % based on 100 wt % of the lubricant composition.


The viscosity modifier may be polyisobutylene or polymethacrylate, and preferably, the viscosity modifier is included in an amount of 0 to 15 wt % based on 100 wt % of the lubricant composition.


The wear-resistant agent may be at least one selected from the group consisting of organic borates, organic phosphites, organic sulfur-containing compounds, zinc dialkyl dithiophosphate, zinc diaryl dithiophosphate and phosphosulfurized hydrocarbon, and preferably, the wear-resistant agent is included in an amount of 0.01 to 3.0 wt %.


The lubricant composition of the present invention has an SRV friction coefficient of 0.1 to 0.35. Moreover, the lubricant composition has a traction coefficient of 0.15 to 0.3.


A better understanding of the present invention through the following examples. However, the present invention is not limited to these examples, but may be embodied in other forms. These examples are provided to thoroughly explain the invention and to sufficiently transfer the spirit of the present invention to those skilled in the art.


1. Preparation of Additive Composition


An additive composition for use in the lubricant composition of the present invention was prepared as shown in Table 2 below.











TABLE 2






Composi-
Composi-


Additive composition
tion A
tion B


















Antioxidant
2,6-dibutylphenol
1
1.5



Diphenylamine
0.8
1


Metal cleaner
Metallic phenate
0.2
0.6


Anticorrosive
Benzotriazole
0.3
1.0


agent


Foam inhibitor
Polyoxyalkylene polyol
0.01
0.02


Pour-point
Polymethacrylate
0.2
0.5


depressant


Viscosity
Polyisobutylene

1.0


modifier


Wear-resistant
Zinc dialkyl dithiophosphate
0.2
1.1


agent









2. Preparation of Liquid Olefin Copolymer


A liquid olefin copolymer was prepared using an oligomerization method through a catalytic reaction process. Depending on the reaction time and conditions, which follow, liquid olefin copolymers having different molecular weights were prepared, and the properties thereof are shown in Table 3 below.


The reaction time and conditions were increased by 4 hr each from 20 hr. Here, the amounts of hydrogen and comonomer C3, which were added thereto, were increased by 10% each, and polymerization was performed under individual conditions, and the resulting polymers were classified depending on the molecular weight thereof.











TABLE 3









Main properties










Alphaolefin
Evaporation
Thickening Power (10
CoE of Thermal


copolymer
Loss (%)
wt % in 150N)
Expansion













Copolymer I
1.28
6
3.00 to 3.20


Copolymer II
0.54
7
3.20 to 3.40


Copolymer III
0.10
8
3.40 to 3.50


Copolymer IV
0.001
10
3.50 to 3.60


Copolymer V
0.0001
12
3.60 to 3.70


Copolymer VI
0.00001
14
3.70 to 3.80









3. Preparation of Lubricant Composition for Hydraulic Oil


A lubricant composition was prepared by mixing a base oil, the liquid olefin copolymer, a phosphorothioate compound, phosphonium phosphate and the additive prepared above, as shown in Tables 4 and 5 below. Here, the base oil was polyalphaolefin (PAO 4 cSt, available from Chevron Philips) having kinematic viscosity of 4 cSt at 1000, and the phosphorothioate compound was monophosphorothioate.


Preparation Examples 1 to 67 and Comparative Examples 1 to 14. Lubricant Composition for Hydraulic Oil Including Additive A














TABLE 4








Phosphorothioate






Alphaolefin
Compound
Phosphonium


Composition
Base oil
copolymer
Monophosphorothioate
phosphate
Additive A




















Preparation
97.135
Copolymer
0.1
0.005
2.71


Example 1

I 0.05


Preparation
96.735
Copolymer
0.5
0.005
2.71


Example 2

I 0.05


Preparation
95.74
Copolymer
1.0
0.5
2.71


Example 3

I 0.05


Preparation
93.74
Copolymer
3.0
0.5
2.71


Example 4

I 0.05


Preparation
88.74
Copolymer
5.0
3.5
2.71


Example 5

I 0.05


Preparation
96.64
Copolymer
0.1
0.05
2.71


Example 6

I 0.5


Preparation
95.74
Copolymer
1.0
0.05
2.71


Example 7

I 0.5


Preparation
93.69
Copolymer
3.0
0.1
2.71


Example 8

I 0.5


Preparation
92.09
Copolymer
0.1
0.1
2.71


Example 9

I 5


Preparation
91.69
Copolymer
0.5
0.1
2.71


Example 10

I 5


Preparation
89.19
Copolymer
3.0
0.1
2.71


Example 11

I 5


Preparation
38.29
Copolymer
5.0
4.0
2.71


Example 12

I 5


Preparation
86.89
Copolymer
0.1
0.3
2.71


Example 13

I 10


Preparation
86.49
Copolymer
0.5
0.3
2.71


Example 14

I 10


Preparation
85.99
Copolymer
1.0
0.3
2.71


Example 15

I 10


Preparation
78.79
Copolymer
5.0
3.5
2.71


Example 16

I 10


Preparation
76.69
Copolymer
0.1
0.5
2.71


Example 17

I 20


Preparation
76.29
Copolymer
0.5
0.5
2.71


Example 18

I 20


Preparation
70.29
Copolymer
5.0
2.0
2.71


Example 19

I 20


Preparation
66.29
Copolymer
0.5
0.5
2.71


Example 20

I 30


Preparation
60.79
Copolymer
5.0
1.5
2.71


Example 21

I 30


Preparation
60.79
Copolymer
0.5
1.0
2.71


Example 22

I 35


Preparation
61.19
Copolymer
1.0
0.1
2.71


Example 23

I 35


Preparation
56.79
Copolymer
3.0
2.5
2.71


Example 24

I 35


Preparation
53.79
Copolymer
5.0
3.5
2.71


Example 25

I 35


Preparation
47.29
Copolymer
10.0 
5.0
2.71


Example 26

I 35


Preparation
47.235
Copolymer
 0.05
0.005
2.71


Example 27

I 50


Preparation
46.285
Copolymer
1.0
0.005
2.71


Example 28

I 50


Preparation
38.79
Copolymer
5.0
3.5
2.71


Example 29

I 50


Preparation
96.64
Copolymer
0.1
0.5
2.71


Example 30

II 0.05


Preparation
95.24
Copolymer
0.5
1.5
2.71


Example 31

II 0.05


Preparation
94.24
Copolymer
1.0
2.0
2.71


Example 32

II 0.05


Preparation
92.24
Copolymer
3.0
2.0
2.71


Example 33

II 0.05


Preparation
90.24
Copolymer
5.0
2.0
2.71


Example 34

II 0.05


Preparation
96.19
Copolymer
0.1
0.5
2.71


Example 35

II 0.5


Preparation
93.29
Copolymer
3.0
0.5
2.71


Example 36

II 0.5


Preparation
83.79
Copolymer
5.0
3.5
2.71


Example 37

II 5


Preparation
78.79
Copolymer
5.0
3.5
2.71


Example 38

II 10


Preparation
72.285
Copolymer
5.0
0.005
2.71


Example 39

II 20


Preparation
97.139
Copolymer
0.1
0.001
2.71


Example 40

III 0.05


Preparation
95.24
Copolymer
0.5
1.5
2.71


Example 41

III 0.05


Preparation
94.24
Copolymer
1.0
2.0
2.71


Example 42

III 0.05


Preparation
92.24
Copolymer
3.0
2.0
2.71


Example 43

III 0.05


Preparation
91.69
Copolymer
0.1
0.5
2.71


Example 44

III 5


Preparation
91.29
Copolymer
0.5
0.5
2.71


Example 45

III 5


Preparation
76.29
Copolymer
0.5
0.5
2.71


Example 46

III 20


Preparation
75.29
Copolymer
1.0
1.0
2.71


Example 47

III 20


Preparation
91.19
Copolymer
0.1
1.0
2.71


Example 48

IV 5


Preparation
88.29
Copolymer
3.0
1.0
2.71


Example 49

IV 5


Preparation
76.69
Copolymer
0.5
0.1
2.71


Example 50

IV 20


Preparation
73.29
Copolymer
3.0
1.0
2.71


Example 51

IV 20


Preparation
92.09
Copolymer
0.1
0.1
2.71


Example 52

V 5


Preparation
91.69
Copolymer
0.5
0.1
2.71


Example 53

V 5


Preparation
78.79
Copolymer
5.0
3.5
2.71


Example 54

V 10


Preparation
77.14
Copolymer
0.1
0.05
2.71


Example 55

V 20


Preparation
76.69
Copolymer
0.5
0.1
2.71


Example 56

V 20


Preparation
68.79
Copolymer
5.0
3.5
2.71


Example 57

V 20


Preparation
45.79
Copolymer
1.0
0.5
2.71


Example 58

V 50


Preparation
43.79
Copolymer
3.0
0.5
2.71


Example 59

V 50


Preparation
42.289
Copolymer
5.0
0.001
2.71


Example 60

V 50


Preparation
93.64
Copolymer
0.1
3.5
2.71


Example 61

VI 0.05


Preparation
93.24
Copolymer
0.5
3.5
2.71


Example 62

VI 0.05


Preparation
92.74
Copolymer
1.0
3.5
2.71


Example 63

VI 0.05


Preparation
92.14
Copolymer
0.1
0.05
2.71


Example 64

VI 5


Preparation
91.69
Copolymer
0.5
0.1
2.71


Example 65

VI 5


Preparation
77.09
Copolymer
0.1
0.1
2.71


Example 66

VI 20


Preparation
76.29
Copolymer
0.5
0.5
2.71


Example 67

VI 20


Comparative
97.24
Copolymer


2.71


Example 1

I 0.05


Comparative
93.74
Copolymer

3.5
2.71


Example 2

II 0.05


Comparative
87.29
Copolymer


2.71


Example 3

II 10


Comparative
73.29
Copolymer

4.0
2.71


Example 4

II 20


Comparative
67.29
Copolymer


2.71


Example 5

II 30


Comparative
87.29
Copolymer
5.0

2.71


Example 6

III 5


Comparative
82.29
Copolymer
5.0

2.71


Example 7

III 10


Comparative
72.29
Copolymer
5.0

2.71


Example 8

III 20


Comparative
88.79
Copolymer

3.5
2.71


Example 9

IV 5


Comparative
87.29
Copolymer
5.0

2.71


Example 10

IV 5


Comparative
82.29
Copolymer
10.0 

2.71


Example 11

IV 5


Comparative
63.79
Copolymer

3.5
2.71


Example 12

V 30


Comparative
58.79
Copolymer

3.5
2.71


Example 13

V 35


Comparative
93.74
Copolymer

3.5
2.71


Example 14

VI 0.05









Preparation Examples 68 to 116 and Comparative Examples 15 to 53. Lubricant Composition for Hydraulic Oil Including Additive B














TABLE 5








Phosphorothioate






Alphaolefin
compound
Phosphonium


Composition
Base oil
copolymer
Monophosphorothioate
phosphate
Additive B




















Preparation
92.58
Copolymer
0.1
0.1
6.72


Example 68

I 0.5


Preparation
92.18
Copolymer
0.5
0.1
6.72


Example 69

I 0.5


Preparation
91.68
Copolymer
1.0
0.1
6.72


Example 70

I 0.5


Preparation
88.08
Copolymer
0.1
0.1
6.72


Example 71

I 5


Preparation
87.28
Copolymer
0.5
0.5
6.72


Example 72

I 5


Preparation
86.78
Copolymer
1.0
0.5
6.72


Example 73

I 5


Preparation
82.68
Copolymer
0.1
0.5
6.72


Example 74

I 10


Preparation
81.78
Copolymer
1.0
0.5
6.72


Example 75

I 10


Preparation
79.78
Copolymer
3.0
0.5
6.72


Example 76

I 10


Preparation
73.08
Copolymer
0.1
0.1
6.72


Example 77

I 20


Preparation
72.28
Copolymer
0.5
0.5
6.72


Example 78

I 20


Preparation
71.78
Copolymer
1.0
0.5
6.72


Example 79

I 20


Preparation
92.18
Copolymer
0.1
0.5
6.72


Example 80

II 0.5


Preparation
88.78
Copolymer
3.0
1.0
6.72


Example 81

II 0.5


Preparation
54.78
Copolymer
5.0
3.5
6.72


Example 82

II 30


Preparation
93.08
Copolymer
0.1
 0.05
6.72


Example 83

III 0.05


Preparation
91.73
Copolymer
0.5
1.0
6.72


Example 84

III 0.05


Preparation
91.23
Copolymer
1.0
1.0
6.72


Example 85

III 0.05


Preparation
89.23
Copolymer
3.0
1.0
6.72


Example 86

III 0.05


Preparation
86.68
Copolymer
0.1
1.5
6.72


Example 87

III 5


Preparation
86.28
Copolymer
0.5
1.5
6.72


Example 88

III 5


Preparation
79.78
Copolymer
5.0
3.5
6.72


Example 89

III 5


Preparation
74.78
Copolymer
5.0
3.5
6.72


Example 90

III 10


Preparation
71.28
Copolymer
0.5
1.5
6.72


Example 91

III 20


Preparation
70.78
Copolymer
1.0
1.5
6.72


Example 92

III 20


Preparation
34.78
Copolymer
5.0
3.5
6.72


Example 93

III 50


Preparation
89.63
Copolymer
0.1
3.5
6.72


Example 94

IV 0.05


Preparation
89.23
Copolymer
0.5
3.5
6.72


Example 95

IV 0.05


Preparation
86.68
Copolymer
0.1
1.5
6.72


Example 96

IV 5


Preparation
83.28
Copolymer
3.0
2.0
6.72


Example 97

IV 5


Preparation
79.78
Copolymer
5.0
3.5
6.72


Example 98

IV 5


Preparation
68.28
Copolymer
3.0
2.0
6.72


Example 99

IV 20


Preparation
72.68
Copolymer
0.5
0.1
6.72


Example 100

IV 20


Preparation
42.68
Copolymer
0.1
0.5
6.72


Example 101

IV 50


Preparation
88.13
Copolymer
0.1
 0.05
6.72


Example 102

V 5


Preparation
87.73
Copolymer
0.5
 0.05
6.72


Example 103

V 5


Preparation
79.78
Copolymer
5.0
3.5
6.72


Example 104

V 5


Preparation
74.78
Copolymer
5.0
3.5
6.72


Example 105

V 10


Preparation
73.08
Copolymer
0.1
0.1
6.72


Example 106

V 20


Preparation
71.78
Copolymer
1.0
0.5
6.72


Example 107

V 20


Preparation
86.73
Copolymer
3.0
3.5
6.72


Example 108

VI 0.05


Preparation
84.73
Copolymer
5.0
3.5
6.72


Example 109

VI 0.05


Preparation
87.68
Copolymer
0.5
0.1
6.72


Example 110

VI 5


Preparation
84.28
Copolymer
3.0
1.0
6.72


Example 111

VI 5


Preparation
68.28
Copolymer
3.0
2.0
6.72


Example 112

VI 20


Preparation
61.28
Copolymer
1.0
1.0
6.72


Example 113

VI 30


Preparation
39.73
Copolymer
 0.05
3.5
6.72


Example 114

VI 50


Preparation
42.28
Copolymer
0.5
0.5
6.72


Example 115

VI 50


Preparation
38.279
Copolymer
5.0
 0.001
6.72


Example 116

VI 50


Comparative
68.28
Copolymer
5.0

6.72


Example 16

III 20


Comparative
58.28
Copolymer
5.0

6.72


Example 17

III 30


Comparative
58.18
Copolymer
0.1

6.72


Example 18

III 35


Comparative
57.78
Copolymer
0.5

6.72


Example 19

III 35


Comparative
57.28
Copolymer
1.0

6.72


Example 20

III 35


Comparative
55.28
Copolymer
3.0

6.72


Example 21

III 35


Comparative
43.18
Copolymer
0.1

6.72


Example 22

III 50


Comparative
42.78
Copolymer
0.5

6.72


Example 23

III 50


Comparative
42.28
Copolymer
1.0

6.72


Example 24

III 50


Comparative
89.73
Copolymer

3.5
6.72


Example 25

IV 0.05


Comparative
92.23
Copolymer
1.0

6.72


Example 26

IV 0.05


Comparative
90.23
Copolymer
3.0

6.72


Example 27

IV 0.05


Comparative
88.23
Copolymer
5.0

6.72


Example 28

IV 0.05


Comparative
87.78
Copolymer

0.5
6.72


Example 29

IV 5


Comparative
78.28
Copolymer
10.0 

6.72


Example 30

IV 5


Comparative
83.28
Copolymer


6.72


Example 31

IV 10


Comparative
78.28
Copolymer
5.0

6.72


Example 32

IV 10


Comparative
39.78
Copolymer

3.5
6.72


Example 33

IV 50


Comparative
42.78
Copolymer
0.5

6.72


Example 34

IV 50


Comparative
42.28
Copolymer
1.0

6.72


Example 35

IV 50


Comparative
40.28
Copolymer
3.0

6.72


Example 36

IV 50


Comparative
38.28
Copolymer
5.0

6.72


Example 37

IV 50


Comparative
93.23
Copolymer


6.72


Example 38

V 0.05


Comparative
93.13
Copolymer
0.1

6.72


Example 39

V 0.05


Comparative
92.73
Copolymer
0.5

6.72


Example 40

V 0.05


Comparative
92.23
Copolymer
1.0

6.72


Example 41

V 0.05


Comparative
90.23
Copolymer
3.0

6.72


Example 42

V 0.05


Comparative
88.23
Copolymer
5.0

6.72


Example 43

V 0.05


Comparative
84.78
Copolymer

3.5
6.72


Example 44

V 5


Comparative
69.78
Copolymer

3.5
6.72


Example 45

V 20


Comparative
63.28
Copolymer


6.72


Example 46

V 30


Comparative
88.28
Copolymer


6.72


Example 47

VI 5


Comparative
78.28
Copolymer
5.0

6.72


Example 48

VI 10


Comparative
58.18
Copolymer
0.1

6.72


Example 49

VI 35


Comparative
57.78
Copolymer
0.5

6.72


Example 50

VI 35


Comparative
57.28
Copolymer
1.0

6.72


Example 51

VI 35


Comparative
55.28
Copolymer
3.0

6.72


Example 52

VI 35


Comparative
53.28
Copolymer
5.0

6.72


Example 53

VI 35









4. Evaluation of Properties


The properties of the lubricant compositions prepared in Preparation Examples and Comparative Examples were measured as follows. The results are shown in Tables 6 and 7 below.


Friction Coefficient


In the ball-on-disc mode, friction performance was evaluated by sequentially elevating the temperature in increments of 100 from 40 to 120□ at 50 Hz and comparing the average friction coefficients at individual temperatures.


Here, the friction coefficient value decreases with an increase in effectiveness.


Traction Coefficient


The traction coefficient was measured using an MTM instrument made by PCS Instruments. Here, the measurement conditions were fixed at 50N and SRR 50%, and friction and traction were observed depending on changes in temperature. The temperature was varied from 40 to 120□, and the average values were compared.


Wear Resistance


Four steel balls were subjected to friction with the lubricant composition for 60 min under conditions of 20 kg load, 1200 rpm, and 540, the sizes of wear scars were compared, and evaluation was carried out in accordance with ASTM D4172. Here, the wear scar (average wear scar diameter, μm) value decreases with an increase in effectiveness.


Oxidation Stability


Oxidation stability was measured using an RBOT (Rotational Bomb Oxidation Test) meter in accordance with ASTM D2271.














TABLE 6









4 Ball
Oxidation



SRV Friction
MTM Traction
Wear
stability



Coefficient
Coefficient
(μm)
(RBOT, min)




















Preparation
0.701
0.598
496
610


Example 1


Preparation
0.732
0.569
477
654


Example 2


Preparation
0.734
0.587
432
523


Example 3


Preparation
0.735
0.544
501
320


Example 4


Preparation
0.712
0.523
665
249


Example 5


Preparation
0.288
0.221
142
1580


Example 6


Preparation
0.285
0.200
152
1650


Example 7


Preparation
0.265
0.236
133
1600


Example 8


Preparation
0.264
0.219
121
1480


Example 9


Preparation
0.267
0.211
110
2000


Example 10


Preparation
0.240
0.236
106
2110


Example 11


Preparation
0.736
0.569
511
333


Example 12


Preparation
0.246
0.222
116
2420


Example 13


Preparation
0.239
0.207
123
1840


Example 14


Preparation
0.257
0.217
140
1680


Example 15


Preparation
0.745
0.564
522
285


Example 16


Preparation
0.258
0.213
146
1590


Example 17


Preparation
0.259
0.243
147
1510


Example 18


Preparation
0.754
0.555
536
278


Example 19


Preparation
0.264
0.222
149
1540


Example 20


Preparation
0.768
0.561
555
269


Example 21


Preparation
0.769
0.532
622
298


Example 22


Preparation
0.774
0.512
654
277


Example 23


Preparation
0.744
0.533
635
279


Example 24


Preparation
0.730
0.612
598
311


Example 25


Preparation
0.741
0.633
590
312


Example 26


Preparation
0.745
0.654
455
322


Example 27


Preparation
0.756
0.687
478
388


Example 28


Preparation
0.725
0.698
497
368


Example 29


Preparation
0.76
0.685
518
384


Example 30


Preparation
0.769
0.696
523
368


Example 31


Preparation
0.778
0.641
537
321


Example 32


Preparation
0.792
0.621
556
325


Example 33


Preparation
0.791
0.632
631
387


Example 34


Preparation
0.269
0.219
106
1650


Example 35


Preparation
0.279
0.245
108
1440


Example 36


Preparation
0.793
0.612
623
345


Example 37


Preparation
0.797
0.587
647
388


Example 38


Preparation
0.755
0.555
612
321


Example 39


Preparation
0.702
0.665
678
654


Example 40


Preparation
0.682
0.610
598
523


Example 41


Preparation
0.713
0.587
599
320


Example 42


Preparation
0.715
0.588
587
333


Example 43


Preparation
0.257
0.219
185
1490


Example 44


Preparation
0.259
0.236
168
2110


Example 45


Preparation
0.278
0.217
135
1580


Example 46


Preparation
0.279
0.213
108
1490


Example 47


Preparation
0.284
0.222
154
1480


Example 48


Preparation
0.231
0.247
163
2456


Example 49


Preparation
0.247
0.278
169
2122


Example 50


Preparation
0.264
0.248
185
2020


Example 51


Preparation
0.255
0.256
154
1854


Example 52


Preparation
0.254
0.219
165
1681


Example 53


Preparation
0.678
0.512
655
279


Example 54


Preparation
0.269
0.213
116
1610


Example 55


Preparation
0.278
0.243
123
1440


Example 56


Preparation
0.744
0.587
478
347


Example 57


Preparation
0.623
0.588
676
348


Example 58


Preparation
0.634
0.521
618
384


Example 59


Preparation
0.709
0.569
589
368


Example 60


Preparation
0.745
0.587
599
348


Example 61


Preparation
0.725
0.555
568
384


Example 62


Preparation
0.756
0.548
534
368


Example 63


Preparation
0.284
0.236
147
2410


Example 64


Preparation
0.291
0.245
149
1810


Example 65


Preparation
0.264
0.247
108
1560


Example 66


Preparation
0.284
0.256
110
1540


Example 67


Comparative
0.721
0.589
454
510


Example 1


Comparative
0.759
0.674
505
348


Example 2


Comparative
0.775
0.555
436
258


Example 3


Comparative
0.811
0.588
698
412


Example 4


Comparative
0.766
0.672
664
510


Example 5


Comparative
0.716
0.521
499
285


Example 6


Comparative
0.717
0.569
580
278


Example 7


Comparative
0.726
0.587
590
269


Example 8


Comparative
0.725
0.611
510
465


Example 9


Comparative
0.691
0.587
651
419


Example 10


Comparative
0.711
0.547
587
322


Example 11


Comparative
0.68
0.563
636
249


Example 12


Comparative
0.7
0.587
597
321


Example 13


Comparative
0.716
0.539
498
396


Example 14





















TABLE 7









4 Ball
Oxidation



SRV Friction
MTM Traction
Wear
stability



Coefficient
Coefficient
(μm)
(RBOT, min)




















Preparation
0.291
0.219
121
1660


Example 68


Preparation
0.268
0.209
122
1640


Example 69


Preparation
0.269
0.236
132
1490


Example 70


Preparation
0.264
0.221
159
2020


Example 71


Preparation
0.247
0.200
164
2110


Example 72


Preparation
0.231
0.236
176
2030


Example 73


Preparation
0.255
0.219
157
1650


Example 74


Preparation
0.254
0.211
161
1580


Example 75


Preparation
0.251
0.236
196
1490


Example 76


Preparation
0.260
0.222
186
1910


Example 77


Preparation
0.269
0.207
193
1480


Example 78


Preparation
0.278
0.222
190
1650


Example 79


Preparation
0.279
0.219
176
1680


Example 80


Preparation
0.284
0.245
189
2020


Example 81


Preparation
0.755
0.587
458
249


Example 82


Preparation
0.798
0.639
655
346


Example 83


Preparation
0.768
0.589
636
347


Example 84


Preparation
0.736
0.598
664
258


Example 85


Preparation
0.747
0.569
673
269


Example 86


Preparation
0.231
0.219
152
1790


Example 87


Preparation
0.255
0.211
169
1560


Example 88


Preparation
0.822
0.587
676
287


Example 89


Preparation
0.813
0.544
618
288


Example 90


Preparation
0.279
0.236
147
2110


Example 91


Preparation
0.278
0.219
146
2020


Example 92


Preparation
0.713
0.555
591
412


Example 93


Preparation
0.693
0.548
587
322


Example 94


Preparation
0.704
0.512
541
368


Example 95


Preparation
0.277
0.245
149
2030


Example 96


Preparation
0.284
0.209
198
1650


Example 97


Preparation
0.715
0.555
612
345


Example 98


Preparation
0.269
0.256
110
1910


Example 99


Preparation
0.264
0.219
121
1480


Example 100


Preparation
0.722
0.589
676
610


Example 101


Preparation
0.291
0.236
132
1680


Example 102


Preparation
0.268
0.221
158
1480


Example 103


Preparation
0.713
0.532
580
365


Example 104


Preparation
0.645
0.555
589
285


Example 105


Preparation
0.255
0.236
194
1610


Example 106


Preparation
0.231
0.211
169
1854


Example 107


Preparation
0.758
0.512
578
321


Example 108


Preparation
0.759
0.563
579
325


Example 109


Preparation
0.251
0.207
154
2080


Example 110


Preparation
0.260
0.234
169
2130


Example 111


Preparation
0.261
0.226
226
1780


Example 112


Preparation
0.275
0.217
169
1790


Example 113


Preparation
0.813
0.613
501
415


Example 114


Preparation
0.734
0.580
512
369


Example 115


Preparation
0.784
0.571
523
358


Example 116


Comparative
0.702
0.569
589
299


Example 16


Comparative
0.682
0.564
597
388


Example 17


Comparative
0.726
0.512
478
347


Example 18


Comparative
0.735
0.533
436
321


Example 19


Comparative
0.749
0.523
505
247


Example 20


Comparative
0.748
0.532
518
258


Example 21


Comparative
0.725
0.621
556
401


Example 22


Comparative
0.704
0.633
623
369


Example 23


Comparative
0.779
0.666
655
358


Example 24


Comparative
0.725
0.555
651
269


Example 25


Comparative
0.779
0.563
523
388


Example 26


Comparative
0.77
0.611
498
396


Example 27


Comparative
0.691
0.587
599
348


Example 28


Comparative
0.711
0.588
568
384


Example 29


Comparative
0.716
0.672
647
346


Example 30


Comparative
0.717
0.499
698
347


Example 31


Comparative
0.745
0.623
612
299


Example 32


Comparative
0.711
0.639
673
519


Example 33


Comparative
0.702
0.598
618
654


Example 34


Comparative
0.632
0.569
589
523


Example 35


Comparative
0.612
0.587
597
320


Example 36


Comparative
0.643
0.547
591
333


Example 37


Comparative
0.756
0.610
698
412


Example 38


Comparative
0.758
0.600
678
415


Example 39


Comparative
0.759
0.588
598
369


Example 40


Comparative
0.76
0.541
599
358


Example 41


Comparative
0.769
0.563
587
347


Example 42


Comparative
0.778
0.522
499
321


Example 43


Comparative
0.715
0.543
590
399


Example 44


Comparative
0.749
0.555
587
321


Example 45


Comparative
0.646
0.569
523
278


Example 46


Comparative
0.76
0.611
624
387


Example 47


Comparative
0.822
0.601
444
412


Example 48


Comparative
0.769
0.587
584
345


Example 49


Comparative
0.778
0.588
562
346


Example 50


Comparative
0.792
0.541
532
347


Example 51


Comparative
0.791
0.513
521
258


Example 52


Comparative
0.793
0.555
511
269


Example 53









As is apparent from Tables 6 and 7, the lubricant compositions including the liquid ethylene alphaolefin copolymer, the phosphorothioate compound and the phosphonium phosphate within the amount ranges of the present invention were significantly reduced in wear scar and friction coefficient compared to the lubricant compositions of Comparative Examples, and also exhibited superior oxidation stability. Therefore, it is concluded that the lubricant composition of the present invention is improved from the aspects of friction characteristics and stability and thus is suitable for use in hydraulic oil.


Although the embodiments of the present invention have been disclosed for illustrative purposes, those skilled in the art will appreciate that various modifications, additions and substitutions are possible, without departing from the scope and spirit of the invention as disclosed in the accompanying claims.

Claims
  • 1. A lubricant composition, comprising: a base oil, a liquid olefin copolymer, a phosphorothioate compound, and phosphonium phosphate.
  • 2. The lubricant composition of claim 1, wherein the liquid olefin copolymer is prepared by copolymerizing ethylene and alphaolefin using a single-site catalyst system.
  • 3. The lubricant composition of claim 1, wherein the phosphorothioate compound is at least one selected from the group consisting of monophosphorothioate, diphosphorothioate, triphosphorothioate, methylphosphorothioate, ethylphosphorothioate, and sulfonylphosphorothioate.
  • 4. The lubricant composition of claim 1, wherein the phosphonium phosphate has a structure of Chemical Formula 7 below.
  • 5. The lubricant composition of claim 2, wherein the single-site catalyst system includes a metallocene catalyst, an organometallic compound and an ionic compound.
  • 6. The lubricant composition of claim 1, wherein the liquid olefin copolymer has a coefficient of thermal expansion of 3.0 to 4.0.
  • 7. The lubricant composition of claim 1, wherein the liquid olefin copolymer has a bromine number of 0.1 or less.
  • 8. The lubricant composition of claim 1, wherein the phosphorothioate compound is included in an amount of 0.1 to 5.0 wt % in the lubricant composition.
  • 9. The lubricant composition of claim 1, wherein the liquid olefin copolymer is included in an amount of 0.5 to 30 wt % in the lubricant composition.
  • 10. The lubricant composition of claim 1, wherein the base oil is at least one selected from the group consisting of mineral oil, polyalphaolefin (PAO), and ester.
  • 11. The lubricant composition of claim 1, further comprising an additive selected from the group consisting of an antioxidant, a metal cleaner, an anticorrosive agent, a foam inhibitor, a pour-point depressant, a viscosity modifier, a wear-resistant agent, and combinations thereof.
  • 12. The lubricant composition of claim 1, wherein the lubricant composition has an SRV friction coefficient of 0.1 to 0.35.
  • 13. The lubricant composition of claim 1, wherein the lubricant composition has a traction coefficient of 0.15 to 0.3.
  • 14. The lubricant composition of claim 1, wherein the lubricant composition endures 1000 min or more in an oxidation stability evaluation (RBOT, ASTM D2271).
  • 15. The lubricant composition of claim 1, wherein the lubricant composition is used as hydraulic oil.
Priority Claims (1)
Number Date Country Kind
10-2019-0023681 Feb 2019 KR national