[0001] The present invention relates to the use of certain additives to extend the thermal
stability and oxidation stability of lubricant compositions, and to lubricant compositions
exhibiting extended thermal stability and oxidation stability.
[0002] Lubricating compositions for antiwear hydraulic and industrial applications typically
contain additive components to impart antiwear performance. Hydraulic grade zinc dialkyldithiophosphates
are typically used in this respect. The compositions usually also contain antioxidant
components. The compositions have conventionally been formulated using Group I base
oils. However, the use of hydrocracked and catalytically dewaxed Group II and Group
III base oils is on the increase. The hydrogenation and dewaxing processes involved
result in base oils of exceptionally low aromaticity and sulphur level. These Group
II and Group III bases have been found to exhibit an improved response to antioxidant
components when compared with Group I basestocks. This has led to the thinking that
use of Group II and Group III bases could allow the level of antioxidants to be decreased
without detriment to the level of antioxidant performance required by end users. However,
rather than leading to reduced amounts of antioxidants being used, the advent of Group
II and Group III base oils has prompted end users to demand a higher level of antioxidant
performance, irrespective of the kind of base oil which is actually used. For example,
whereas a performance level of 2000 to 4000 hours in the ASTM D943 thermal oxidation
test was previously acceptable, extended performance is now commonly required, for
instance a result of 10,000 hours in the ASTM D943 test.
[0003] In accordance with the present invention it has now been found that specific antioxidant
components, and combinations thereof, can be blended in lubricant compositions containing
hydraulic antiwear components to achieve extended thermal and oxidative stability
without formation of sludge. More particularly, the combinations have been found to
give improved thermal stability, and thus reduced levels of sludge, when used in Group
I, II and III basestocks and increased oxidation stability in Group II, or higher
basestocks. These advantageous results enables a variety of base oils to be are used
in formulating the lubricant composition and, in turn, this allows industrial formulators
enhanced flexibility whilst also meeting the now extended performance requirements
of end users.
[0004] Accordingly, the present invention provides the use in a lubricant composition comprising
a hydraulic antiwear component and a base oil of an additive comprising at least one
amine antioxidant and at least one additional antioxidant selected from ashless dithiocarbamate,
sulphurised olefin and phenolic, antioxidants to provide a lubricant having improved
thermal stability and oxidative stability in all basestock types.
[0005] The performance of the combinations of antioxidants used in accordance with the present
invention will vary depending, amongst other things, on the base oil type, the specific
combination and the concentration of additive(s), used. In terms of thermal stability
the additives used in accordance with the present invention enable formulation of
lubricants which may avoid excessive sludge formation after a period of 10 days when
the lubricant is tested in accordance with the NOC test and when the base oil used
is a Group I basestock. In a preferred embodiment the amount of sludge produced after
10 days in this test is not more than 100 mg/100 ml, preferably not more than 25 mg/
100 ml. A 10 day sludge result of less than 10 mg/100 ml is particularly preferred.
In terms of oxidation stability the additives used in accordance with the present
invention typically enable formulation of lubricants which use a Group II or higher
basestock and which give a result of at least 500 minutes, preferably at least 600
minutes, in the RBOT thermal stability test. Thus, the present invention relates to
combinations of antioxidants which may be used to achieve good oxidation performance
in Group II or higher basestock without derating thermal stability performance when
Group I or higher basestock is used, and vice versa.
[0006] The amine used in the present invention is selected from optionally alkylated diphenylamines,
phenyl-naphthylamines and mixtures thereof. Examples of such components that may be
used in this invention include, but are not limited to, diphenylamine, phenyl-α-naphthylamine,
phenyl-beta-naphthylamine, butyldiphenylamine, dibutyldiphenylamine, octyldiphenylamine,
dioctyldiphenylamine, nonyldiphenylamine, dinonyldiphenylamine, dioctyldiphenylamine,
nonyldiphenylamine, dinonyldiphenylamine, heptyldiphenylamine, diheptyldiphenylamine,
methylstyryldiphenylamine, mixed butyl/octyl alkylated diphenylamines, mixed butyl/styryl
alkylated diphenylamines, mixed nonyl/ethyl alkylated diphenylamines, mixed octyl/styryl
alkylated diphenylamines, mixed ethyl/methylstyryl alkylated diphenylamines, octyl
alkylated phenyl-α-naphthylamines and mixed alkylated phenyl-α-naphthylamines. 2,6-di-t-butyl-α-dimethylamino-p-cresol
may also be used.
[0007] Useful amine antioxidants are generally characterized by their nitrogen content and
TBN as determined by ASTM D 2896. It is preferred that the nitrogen content of the
amine antioxidants be between 3.0 and 7.0 wt% and the TBN be between 100 and 250 mg
KOH/g of the neat, i.e. undiluted, component.
[0008] The concentration of amine antioxidant(s) in the finished composition varies depending
upon the basestock used, customer requirements and applications. Typically, the total
amount of amine antioxidant present in the finished composition is from 0.04 wt% to
0.4 wt%, preferably, from 0.05 wt% to 0.2 wt %.
[0009] The sulphur-containing compounds of the present invention are selected from the group
consisting of sulphurized olefins, sulphurized fatty acids, ashless dithiocarbamates,
tetraalkylthiuram disulphides and mixtures thereof. The sulphurized olefins suitable
for use in the present invention may be prepared by a number of known methods. They
are typically characterized by the type of olefin used in their production and their
final sulphur content. High molecular weight olefins (e.g., those having an average
molecular weight (Mn) of from about 112 to about 351 g/mole) are preferred. Examples
of olefins that may be used include α-olefins, isomerized α-olefins, branched olefins,
cyclic olefins, polymeric olefins and mixtures thereof Examples of α-olefins that
may be used include 1-butene, 1-pentene, 1-hexene, 1-heptene, 1-octene, 1-nonene,
1-decene, 1-undecene, 1-dodecene, 1-tridecene, 1-tetradecene, 1-pentadecene, 1-hexadecene,
1-heptadecene, 1-octadecene, 1-nonadecene, 1-eicosene, 1-heneicosene, 1-docosene,
1-tricosene, 1-tetracosene, 1-pentacosene and mixtures thereof. α-Olefins may be isomerized
before the sulphurization reaction or during the sulphurization reaction. Structural
and/or conformational isomers of the α-olefins that contain internal double bonds
or branching may also be used. For example, isobutylene is the branched olefin counterpart
of the α-olefin 1-butene.
[0010] Sulphur sources that may be used in the sulphurization reaction can include, for
example, elemental sulphur, sulphur monochloride, sulphur dichloride, sodium sulphide,
sodium polysulphide, and mixtures thereof added together or at different stages of
the sulphurization process.
[0011] Unsaturated fatty acids and oils, because of their unsaturation, may also be sulphurized
and used in this invention. Examples of fatty acids that may be used include lauroleic
acid, myristoleic acid, palmitoleic acid, oleic acid, elaidic acid, vaccenic acid,
linoleic acid, linolenic acid, gadoleic acid, arachidonic acid, erucic acid, and mixtures
of these. Examples of oils or fats that may be used include corn oil, cottonseed oil,
grapeseed oil, olive oil, palm oil, peanut oil, rapeseed oil, safflower seed oil,
sesame seed oil, soybean oil, sunflower oil, sunflower seed oil, and combinations
thereof.
[0012] Examples of ashless dithiocarbamates that may be used include, but are not limited
to, methylene-bis(dialkyldithiocarbamate), ethylene-bis(dialkyldithiocarbamate), and
isobutyl disulphide-2,2'-bis(dialkyldithiocarbamate), where the alkyl groups of the
dialkyldithiocarbamate can preferably have from 1 to 16 carbons. Examples of preferred
ashless dithiocarbamates are methylene-bis(dibutyldithiocarbamate), ethylene-bis (dibutyldithiocarbamate),
and isobutyl disulphide-2,2
'-bis(dibutyldithiocarbamate). Examples of preferred tetraalkylthiuram disulphides
that may be used include tetrabutylthiuram disulphide and tetraoctylthiuram disulphide.
[0013] The concentration of the sulphur-containing compound in the finished composition
can vary depending upon the customers' requirements and applications. The compound
is typically used in an amount of upto 0.1% by weight, preferably upto 0.05% by weight
based on the total weight of the lubricant composition. An important criteria for
selecting the concentration of the compound is the sulphur content. The compound should
typically deliver between 0.005 wt. % and 0.07 wt. % of sulphur to the finished composition.
For example, a sulphurized olefin having 12 wt. % sulphur content should be used between
0.04 wt. % and 0.58 wt. % to deliver between 0.005 wt. % and 0.07 wt. % sulphur to
the finished composition. An ashless dithiocarbamate having 30 wt. % sulphur content
should be used between 0.02 wt. % and 0.23 wt. % to deliver between 0.005 wt. % and
0.07 wt. % sulphur to the finished composition.
[0014] Another criterion useful for selecting the sulphur-containing compound is the content
of active sulphur as determined by ASTM D 1662. The presence of high levels of active
sulphur can lead to significant corrosion and sludge problems in the finished lubricant.
In a preferred embodiment of the present invention, the level of active sulphur in
the compound is below 1.5 wt. % as determined by ASTM D 1662.
[0015] An example of a sulphurized olefin that may be used in this invention would contain
approximately 12 wt. % total sulphur content and <1 wt. % active sulphur. Examples
of commercially available sulphurized fatty oils or mixtures of sulphurized fatty
oils and olefins, that may be used in this invention include those having approximately
9.5 wt. % sulphur content and 1 wt. % active sulphur, approximately 12.5 wt. % sulphur
content and 1.5 wt. % active sulphur, and approximately 10 wt. % sulphur content and
<1 wt. % active sulphur. An example of an ashless dithiocarbamate that may be used
in this invention would be one which has approximately 30 wt. % sulphur from a practical
standpoint the sulphur-containing compound should contain a minimum of 8.0 wt% sulphur
in order to minimize the amount of additive needed to deliver the required amount
of sulphur.
[0016] Mixtures of sulphurized olefins, ashless dithiocarbamates and tetraalkylthiuram disulphides,
in varying proportions, may also be used, as long as the desired total sulphur content,
and active sulphur content are satisfied.
[0017] Examples of phenolic antioxidants which may be used include hindered phenolics such
as 2,6-di-butylphenol, 4-methyl-2,6-di-t-butylphenol, 2,4,6-tributylphenol, 2-t-butylphenol,
2,6-diisopropylphenol, 2-methyl-6-t-butylphenol, 2,4-dimethyl-6-t-butylphenol, 4-(N,N-dimethylaminomethyl)-2,6-di-t-butylphenol,
4-ethyl-2,6-di-t-butylphenol, 2-methyl-6-styrylphenol, 2,6-di-styryl-nonylphenol and
mixtures thereof. Also useful are methylene bridged alkyl phenols and these may be
used singly or in combination with each other or with sterically hindered unbridged
phenols. Examples include 4,4'-methylene-bis(2,6-di-butylphenol), 4,4'-methylene-bis
(6-t-butyl-o-cresol), 4,4'-methylene-bis(2-t-amyl-o-cresol), 2,2'-methylene-bis(4-methyl-6-t-butylphenol),
methylene bridged t-butylphenol mixtures, iso-octyl-3,5-di-butyl-4-hydroxy hydrocinnamate
and thiodiethylene-bis (3,5-di-butyl-4-hydroxy)hydrocinnamate. Also useful are mixtures
of methylene bridged alkyl phenols such as described in USP 3,211,652. Typically,
the phenolic antioxidant will be present in the finished lubricant in an amount of
upto 0.4% by weight, preferably upto 0.15% by weight.
[0018] The present invention also provides lubricant compositions, as described herein,
comprising a hydraulic antiwear component, a base oil, at least one amine antioxidant
and at least one additional antioxidant.
[0019] The antioxidants useful in the present invention are commercially available or may
be prepared by the application or adaptation of known techniques.
[0020] Usually, the hydraulic antiwear additive used in the composition of the invention
is a hydraulic grade zinc dialkyldithiophosphate (ZDDP). "Hydraulic grade" means that
the antiwear component is suitable for use in hydraulic applications, particularly
with respect to their thermal stability. (ZDDPs) which have insufficient thermal stability
tend to degrade rapidly to breakdown products which can be corrosive, in particular
towards copper. This is a serious problem as certain hydraulic system components are
made of this metal. Furthermore, the breakdown products can cause sludge formation
which in turn can result in filter blocking. Thus, not all types of ZDDPs are suitable
for use in the present invention. Zinc dihydrocarbyl dithiophosphates which may be
used in the present invention are well-known in the art (see for example U.S. Pat.
No. 4,101,429). Suitably the zinc dihydrocarbyl dithiophosphate is a zinc dialkyl
dithiophosphate typically containing about 4 to about 12 carbon atoms and more commonly
about 6 to about 12 carbon atoms in each alkyl group. Preferably each alkyl group
contains about 8 to about 12 carbon atoms. Examples of suitable alkyl moieties include
butyl, sec-butyl, isobutyl, tert-butyl, pentyl, n-hexyl, sec-hexyl, n-octyl, 2-ethylhexyl,
decyl and dodecyl. Preferably each alkyl moiety is 2-ethylhexyl. Zinc dialkyl dithiophosphates
of this type are described in European patent application no. 95306722.0 and are commercially
available.
[0021] The ZDDP may be used in the lubricant over a broad weight range. It is usual however
that the lubricant contains about 0.4 to about 0.9% by weight ZDDP. Preferably, the
fluid comprises 0.6% by weight ZDDP.
[0022] It is generally possible to characterise those ZDDPs which are useful in the present
invention by reference to their overbased to neutral ratio or by their titratable
base number (TBN). Useful ZDDPs typically exhibit an overbased to neutral ratio of
from 0.3:1 to 2:1, preferably 0.5:1 to 2:1. ZDDPs having an overbased to neutral ratio
of about 1:1 are more commonly used. The ratio in question is determined by
31P nmr. In terms of TBN, useful ZDDPs generally exhibit a minimum value of about 10
mgKOH/g and preferably about 12 mgKOH/g. ZDDPs having a TBN of about 15 mgKOH/g are
more commonly used. TBN is determined in accordance with ASTM D664.
[0023] Alternatively, it is generally possible to characterise ZDDPs which may be used by
reference to the thermal stability of the finished hydraulic fluid in which they are
included. Here reference may be made to the ASTM D2619 and CCM "A" thermal stability
tests. To meet the requirements of the ASTM D2619 test the finished fluid should give
a maximum copper loss of 0.2 mg. To pass the CMC "A" test the finished fluid should
give a maximum copper rod rating of 5 and a maximum sludge deposit of 25 mg/100 ml.
The ASTM D2619 and CCM "A" tests are well known in the art.
[0024] It is possible to further improve the thermal stability of the lubricant composition
by post-treatment of the ZDDP component using a zinc alkanoate. Typically the alkanoate
is branched on its β-carbon atom. Such components are also described in European patent
application no. 95306722.0. The use of zinc octanoate is preferred, especially an
overbased zinc octanoate such as zinc octanoate 22% which is commercially available
under this designation.
[0025] In an embodiment of the invention the amine antioxidant is phenyl-α-naphthylamine
or 2,6-di-t-butyl-α-dimethylamino-p-cresol, alone or each in combination with diphenylamine.
Combinations based on phenyl-α-naphthylamine and diphenylamine are preferred.
[0026] Preferred combinations of antioxidants include: phenyl-α-naphthylamine, diphenylamine
and an ashless dithiocarbamate, such as methylene-bis(dibutyldithiocarbamate); phenyl-α-naphthylamine,
diphenylamine and a phenolic antioxidant, such as 2,6-di-t-butylphenol; and phenyl-α-naphthylamine,
diphenylamine and a sulphurised olefin, such as one derived from a mixture of C
16-18 isomerised α-olefins. In these combinations the phenyl-α-naphthylamine may be replaced
by 2,6-di-t-butyl-α-dimethylamino-p-cresol.
[0027] Lubricating oils contemplated for use in this invention include natural lubricating
oils, synthetic lubricating oils and mixtures thereof. Suitable lubricating oils also
include basestocks obtained by isomerization of synthetic wax and slack wax, as well
as basestocks produced by hydrocracking (rather than solvent extracting) the aromatic
and polar components of crude oil. In general, both the natural and synthetic lubricating
oils will each have a kinematic viscosity ranging from about 1 x 10
-6 m
2/s to about 40 x 10
-6 m
2/s (about 1 to about 40 cSt) at 100°C, although typical applications will require
each oil to have a viscosity ranging from about 2 x 10
-6 m
2/s to about 8 x 10
-6 m
2/s (about 2 to about 8 cSt) at 100°C.
[0028] Natural base oils include animal oils, vegetable oils (e.g., castor oil and lard
oil), petroleum oils, mineral oils, and oils derived from coal or shale. The preferred
natural base oil is mineral oil.
[0029] The mineral oils useful in this invention include all common mineral oil base stocks.
This would include oils that are naphthenic or paraffinic in chemical structure. Oils
that are refined by conventional methodology using acid, alkali, and clay or other
agents such as aluminum chloride, or they may be extracted oils produced, for example,
by solvent extraction with solvents such as phenol, sulphur dioxide, furfural, dichlordiethyl
ether, etc. They may be hydrotreated or hydro-refined, dewaxed by chilling or catalytic
dewaxing processes, or hydrocracked. The mineral oil may be produced from natural
crude sources or be composed of isomerized wax materials or residues of other refining
processes.
[0030] Typically the mineral oils will have kinematic viscosities of from 2 x 10
-6 m
2/s to 12 x 10
-6 m
2/s (2 cSt to 12 cSt) at 100°C. The preferred mineral oils have kinematic viscosities
of from 3 x 10
-6 m
2/s to 10 x 10
-6 m
2/s (3 to 10 cSt), and most preferred are those mineral oils with viscosities of 5
x 10
-6 m
2/s to 9 x 10
-6 m
2/s (5 to 9 cSt) at 100°C.
[0031] Synthetic lubricating oils useful in this invention include hydrocarbon oils and
halo-substituted hydrocarbon oils such as oligomerized, polymerized, and interpolymerized
olefins [e.g., polybutylenes, polypropylenes, propylene, isobutylene copolymers, chlorinated
polylactenes, poly(1-hexenes), poly(1-octenes), and mixtures thereof]; alkylbenzenes
[e.g., polybutylenes, polypropylenes, propylene, isobutylene copolymers, chlorinated
polylactenes, poly(1-hexenes), poly (1-octenes) and mixtures thereof]; alkylbenzenes
[e.g., dodecyl-benzenes, tetradecylbenzenes, dinonyl-benzenes and di(2-ethylhexyl)benzene];
polyphenyls [e.g., biphenyls, terphenyls, alkylated polyphenyls]; and alkylated diphenyl
ethers, alkylated diphenyl sulphides, as well as their derivatives, analogs, and homologs
thereof, and the like. The preferred synthetic oils are oligomers of α-olefins, particularly
oligomers of 1-decene, also known as polyalpha olefins or PAO's.
[0032] Synthetic lubricating oils also include alkylene oxide polymers, interpolymers, copolymers,
and derivatives thereof where the terminal hydroxyl groups have been modified by esterification
or etherification. This class of synthetic oils is exemplified by: polyoxyalkylene
polymers prepared by polymerization of ethylene oxide or propylene oxide; the alkyl
and aryl ethers of these polyoxyalkylene polymers (e.g., methyl-polyisopropylene glycol
ether having an average molecular weight of 1000, diphenyl ether of polypropylene
glycol having a molecular weight of 100-1500); and mono- and poly-carboxylic esters
thereof (e.g., the acetic acid esters, mixed C
3-C
8 fatty acid esters, and C
12 oxo acid diester of tetraethylene glycol).
[0033] Another suitable class of synthetic lubricating oils comprises the esters of dicarboxylic
acids (e.g., phthalic acid, succinic acid, alkyl succinic acids and alkenyl succinic
acids, maleic acid, azelaic acid, suberic acid, sebacic acid, fumaric acid, adipic
acid, linoleic acid dimer, malonic acid, alkylmalonic acids and alkenyl malonic acids)
with a variety of alcohols (e.g., butyl alcohol, hexyl alcohol, dodecyl alcohol, 2-ethylhexyl
alcohol, ethylene glycol, diethylene glycol monoethers and propylene glycol). Specific
examples of these esters include dibutyl adipate, di(2-ethylhexyl) sebacate, di-n-hexyl
fumarate, dioctyl sebacate, diisooctyl azelate, diisodecyl azelate, dioctyl isophthalate,
didecyl phthalate, dieicosyl sebacate, the 2-ethylhexyl diester of linoleic acid dimer,
and the complex ester formed by reacting one mole of sebacic acid with two moles of
tetraethylene glycol and two moles of 2-ethyl-hexanoic acid. A preferred type of oil
from this class of synthetic oils are adipates of C
4 to C
12 alcohols.
[0034] Esters useful as synthetic lubricating oils also include those made from C
5 to C
12 monocarboxylic acids and polyols and polyol ethers such as neopentyl glycol, trimethylolpropane
pentaerythritol, dipentaerythritol and tripentaerythritol.
[0035] Silicon-based oils (such as the polyalkyl-, polyaryl-, polyalkoxy-, or polyaryloxy-siloxane
oils and silicate oils) comprise another useful class of synthetic lubricating oils.
These oils include tetra-ethyl silicate, tetraisopropyl silicate, tetra-(2-ethylhexyl)
silicate, tetra-(4-methyl-2-ethylhexyl) silicate, tetra-(p-tert-butylphenyl) silicate,
hexa-(4-methyl-2-pentoxy)-disiloxane, poly(dimethyl)-siloxanes and poly (methylphenyl)
siloxanes. Other synthetic lubricating oils include liquid esters of phosphorus containing
acids (e.g., tricresyl phosphate, trioctylphosphate, and diethyl ester of decylphosphonic
acid), polymeric tetra-hydrofurans and poly-α-olefins.
[0036] The lubricating base oils may be derived from refined, re-refined oils, or mixtures
thereof. Unrefined oils are obtained directly from a natural source or synthetic source
(e.g., coal, shale, or tar sands bitumen) without further purification or treatment.
Examples of unrefined oils include a shale oil obtained directly from a retorting
operation, a petroleum oil obtained directly from distillation, or an ester oil obtained
directly from an esterification process, each of which is then used without further
treatment. Refined oils are similar to the unrefined oils except that refined oils
have been treated in one or more purification steps to improve one or more properties.
Suitable purification techniques include distillation, hydrotreating, dewaxing, solvent
extraction, acid or base extraction, filtration, and percolation, all of which are
known to those skilled in the art. Re-refined oils are obtained by treating used oils
in processes similar to those used to obtain the refined oils. These re-refined oils
are also known as reclaimed or reprocessed oils and are often additionally processed
by techniques for removal of spent additives and oils breakdown products. White oils,
as taught in U.S. 5,736,490 may also be used as the base oil, especially for turbine
applications.
[0037] In an embodiment of the invention the base oil is a Group I, Group II or Group III
base oil. The use of Group II or Group III base oils is preferred.
[0038] The American Petroleum Institute has categorized these different basestock types
as follows: Group I, >0.03 wt% sulphur, and/or <90 vol% saturates, viscosity index
between 80 and 120; Group II, ≤0.03 wt% sulphur, and ≥ 90 vol% saturates, viscosity
index between 80 and 120; Group III, ≤ 0.03 wt% sulphur, and ≥ 90 vol% saturates,
viscosity index >120; Group IV, all polyalphaolefins. Hydrotreated basestocks and
catalytically dewaxed basestocks, because of their low sulphur and aromatics content,
generally fall into the Group II and Group III categories. Polyalphaolefins (Group
IV basestocks) are synthetic base oils prepared from various α-olefins and are substantially
free of sulphur and aromatics.
[0039] The lubricant composition of the present invention may be prepared by simple blending
of the various components with a suitable base oil.
[0040] For the sake of convenience, and in another embodiment of the present invention,
the additive components used in practice of this invention may be provided as a concentrate
for formulation into a lubricant composition ready for use.
[0041] The concentrate may comprise, in addition to the fluid components, a solvent or diluent
for the fluid components. The solvent or diluent should be miscible with and/or capable
of dissolving in the base oil to which the concentrate is to be added. Suitable solvents
and diluents are well known. The solvent or diluent may be the base oil of the lubricating
oil composition itself. The concentrate may suitably include any of the conventional
additives used in lubricating oils compositions. The proportions of each component
in the concentrate are controlled by the intended degree of dilution, though top treatment
of the formulated fluid is possible.
[0042] Other additives commonly used in lubricants/fluids for turbine, antiwear hydraulic
and industrial applications may be included in the compositions or concentrates of
the present invention. These include demulsifiers, corrosion inhibitors, dispersants,
sulphur- and/or phosphorus-containing antiwear agents and rust inhibitors. These additives,
when present, are used in amounts conventionally used in such applications. Some additives
may be included in the concentrate and some added to the fully formulated lubricant/fluid
as a top-treat.
[0043] The invention will now be illustrated by the following Examples that are not intended
to limit the scope of the invention in any way.
EXAMPLES
[0044] A lubricant composition was prepared by blending components in the proportions specified
in the following table.
| Component |
% by weight |
| Corrosion inhibitor |
0.0085 |
| Detergent |
0.050 |
| Rust inhibitor |
0.051 |
| Phenolic antioxidant |
0.013 |
| Demulsifier |
0.0064 |
| Process oil |
0.0111 |
| *ZDDP |
0.510 |
| Base oil |
Balance to 100% |
[0045] The ZDDP was zinc di(2-ethylhexyl)dithiophosphate.
[0046] The base oil used was either a Group I or Group II base oil. Further details of this
are given in the following table.
1. Use, in a lubricant composition comprising a hydraulic antiwear component and a base
oil, of an additive comprising an amine antioxidant and at least one additional antioxidant
selected from ashless dithiocarbamate, sulphurised olefin and phenolic, antioxidants
to provide a lubricant having improved thermal and oxidation stability.
2. Use according to claim 1, wherein the antiwear component is a hydraulic grade zinc
dialkyldithiophosphate.
3. Use according to claim 1 or claim 2, wherein the base oil is a Group I basestock.
4. Use according to claim 1 or 2, wherein the base oil is a Group II or Group III basestock.
5. Use according to any one of claims 1 to 4, wherein the additive comprises diphenylamine
and phenyl-α-naphthylamine.
6. Use according to any one of claims 1 to 4, wherein the additive comprises diphenylamine
and 2,6-di-t-butyl-α-dimethylamino-p-cresol.
7. Use according to any one of claims 1 to 6, wherein the phenolic antioxidant is 2,6-di-t-butylphenol.
8. Use according to any one of claims 1 to 6, wherein the sulphurised olefin is derived
from a mixture of C16-18 isomerised α-olefins.
9. Use according to any one of claims 1 to 6, wherein the ashless dithiocarbamate is
methylene-bis(di-butyldithiocarbamate).
10. Use according to any one of the preceding claims, wherein the total amount of amine
antioxidant is from 0.04 to 0.4 wt% based on the total weight of the lubricant.
11. A lubricant composition comprising a hydraulic antiwear component, a base oil, at
least one amine antioxidant and at least one antioxidant selected from ashless dithiocarbamate,
sulphurised olefin and phenolic, antioxidants.
12. A composition according to claim 11, wherein the additive is as defined in any one
of claims 5 to 9.
13. A composition according to claim 11 or 12, wherein the total amount of amine antioxidant
is from 0.04 to 0.4 % by weight based on the total weight of the composition.