FIELD OF THE INVENTION
[0001] The invention is directed to additive concentrates useful in the preparation of lubricating
oil compositions. More specifically, preferred embodiments of the present invention
provide lubricating oil additive concentrates exhibiting improved storage stability.
BACKGROUND OF THE INVENTION
[0002] Lubricating oil compositions for use in crankcase engine oils comprise a major amount
of base stock oil and minor amounts of additives that improve the performance and
increase the useful life of the lubricant. Crankcase lubricating oil compositions
conventionally contain basic metal complexes, which act as detergents and acid neutralizers,
phenolic and/or aminic antioxidants and organic friction modifiers containing at least
one hydroxyl or amino group, which function as organic friction modifiers that are
effective in improving fuel economy. In the face of increased demands for improved
fuel economy, and further demands for reductions in the amounts of metal (ash) contained
in the lubricant, formulators have used ever-increasing amounts of organic friction
modifiers.
[0003] Lubricating oil additives are commonly provided to lubricant formulators in the form
of 10 to 80 mass %, e.g., 20 to 80 mass % active ingredient (AI) concentrates, which
are then dissolved in major amounts of oil of lubricating viscosity to provide a fully
formulated lubricant. The concentrates are commonly diluted in 3 to 100, e.g., 5 to
40 parts by weight of oil of lubricating viscosity, per part by weight of the additive
concentrate. As noted above, certain lubricating oil additives are known to interact
with others in concentrates. One such known interaction occurs between organic friction
modifiers and overbased metal detergents. Specifically, the organic friction modifiers
have been found to adversely affect the complex of the metal detergents, causing the
formation of sediment in the concentrate upon storage. Previously, this interaction
has been minimized by selecting detergents that did not severely interact with the
organic friction modifier. The addition of a polyalkenyl acylating agent has also
been found to regulate this unwanted interaction. However, the detergents less likely
to interact with organic friction modifiers have been found to cause gelation problems
in additive packages, and the presence of polyalkenyl acylating agents (e.g., polyisobutenyl
succinic anhydride (PIBSA)) has been found to negatively impact the fuel economy potential
of lubricating oil compositions. Further, with the increased amounts of the organic
friction modifier now required, the effect of polyalkenyl acylating agent compatibilizers
and detergent selection on additive package stability has become insufficient.
[0004] As lubricating oil quality standards have become more stringent, the required amount
of organic friction modifier has increased, and the presence of even minor amounts
of sediment in additive concentrates has become unacceptable to lubricant formulators.
Therefore, it would be advantageous to be able to provide additive concentrates containing
overbased metal detergents and high levels of organic friction modifiers, in which
the components do not interact to form sediment.
SUMMARY OF THE INVENTION
[0005] The present invention provides a lubricant additive concentrate comprising an admixture
of at least one basic metal complex, at least 1.7 mass %, based on the mass of the
condensate, of at least one organic friction modifier having at least one hydroxyl
or amino group, and an oil-soluble hydrocarbyl phenol aldehyde condensate.
[0006] The oil-soluble hydrocarbyl phenol aldehyde condensate is preferably a methylene
bridged alkyl phenol. The presence of the oil-soluble, hydrocarbyl phenol aldehyde
condensate improves concentrate stability.
[0007] In accordance with another aspect of the present invention, there is provided a method
of improving the stability of a lubricant additive concentrate comprising an admixture
of at least one basic metal complex and at least one organic friction modifier having
at least one hydroxyl or amino group, which method comprises adding to said concentrate
a hydrocarbyl phenol aldehyde condensate. The hydrocarbyl phenol aldehyde condensate
is preferably a methylene bridged alkyl phenol.
[0008] Other and further objects, advantages and features of the present invention will
be understood by reference to the following specification.
DETAILED DESCRIPTION OF THE INVENTION
[0009] Organic friction modifiers useful in the practice of the invention, include oil-soluble
compounds containing at least one polar group selected from hydroxyl and amine groups,
which compounds are capable of reducing friction under hydrodynamic and mixed hydrodynamic/boundary
layer conditions. Examples of such materials include glycerol esters of higher fatty
acids, for example, glycerol mono-oleate; esters of long chain polycarboxylic acids
with diols, for example, the butane diol ester of a dimerized unsaturated fatty acid;
oxazoline compounds; and alkoxylated alkyl-substituted mono-amines, diamines and alkyl
ether amines, for example, ethoxylated tallow amine and ethoxylated tallow ether amine.
Particularly preferred organic friction modifiers include glycerol oleates, particularly
glycerol monooleate, and ethoxylated amines, particularly ethoxylated tallow amine.
Because adverse interactions are more severe when elevated levels of organic friction
modifier are present in the concentrate, the concentrate of the present invention
contains at least 1.7 mass %, preferably at least 3 mass %, and more preferably at
least 5 mass %, of organic friction modifier, based on the total weight of the additive
concentrate. In alternative terms, concentrates that contain the organic friction
modifier in an amount sufficient to provide a formulated lubricant with at least 0.15
mass %, preferably, at least 0.25 mass % and more preferably at least 0.5 mass % of
organic friction modifier after dilution are preferred.
[0010] Basic metal complexes useful in the context of the invention function as both detergents
to reduce or remove deposits and as acid neutralizers or rust inhibitors, thereby
reducing wear and corrosion and extending engine life. Detergents generally comprise
a polar head with a long hydrophobic tail. The polar head comprises a metal salt of
an acidic organic compound. The salts may contain a substantially stoichiometric amount
of the metal in which case they are usually described as normal or neutral salts,
and would typically have a total base number or TBN (as can be measured by ASTM D2896)
of from 0 to 80. A large amount of a metal base may be incorporated by reacting excess
metal compound (e.g., an oxide or hydroxide) with an acidic gas (e.g., carbon dioxide).
The resulting overbased detergent comprises neutralized detergent as the outer layer
of a metal base (e.g. carbonate) micelle. Such overbased detergents may have a TBN
of 150 or greater, and typically will have a TBN of from 250 to 450 or more.
[0011] Detergents that may be used include oil-soluble neutral and overbased sulfonates,
phenates, sulfurized phenates, thiophosphonates, salicylates, and naphthenates and
other oil-soluble carboxylates of a metal, particularly the alkali or alkaline earth
metals, e.g., barium, sodium, potassium, lithium, calcium, and magnesium. The most
commonly used metals are calcium and magnesium, which may both be present in detergents
used in a lubricant, and mixtures of calcium and/or magnesium with sodium. Particularly
convenient metal detergents are neutral and overbased calcium sulfonates having TBN
of from 20 to 450, neutral and overbased calcium phenates and sulfurized phenates
having TBN of from 50 to 450 and neutral and overbased magnesium or calcium salicylates
having a TBN of from 20 to 450. Combinations of detergents, whether overbased or neutral
or both, may be used.
[0012] Sulfonates may be prepared from sulfonic acids which are typically obtained by the
sulfonation of alkyl substituted aromatic hydrocarbons such as those obtained from
the fractionation of petroleum or by the alkylation of aromatic hydrocarbons. Examples
included those obtained by alkylating benzene, toluene, xylene, naphthalene, diphenyl
or their halogen derivatives such as chlorobenzene, chlorotoluene and chloronaphthalene.
The alkylation may be carried out in the presence of a catalyst with alkylating agents
having from about 3 to more than 70 carbon atoms. The alkaryl sulfonates usually contain
from about 9 to about 80 or more carbon atoms, preferably from about 16 to about 60
carbon atoms per alkyl substituted aromatic moiety.
[0013] The oil soluble sulfonates or alkaryl sulfonic acids may be neutralized with oxides,
hydroxides, alkoxides, carbonates, carboxylate, sulfides, hydrosulfides, nitrates,
borates and ethers of the metal. The amount of metal compound is chosen having regard
to the desired TBN of the fmal product but typically ranges from about 100 to 220
mass % (preferably at least 125 mass %) of that stoichiometrically required.
[0014] Metal salts of phenols and sulfurized phenols are prepared by reaction with an appropriate
metal compound such as an oxide or hydroxide and neutral or overbased products may
be obtained by methods well known in the art. Sulfurized phenols may be prepared by
reacting a phenol with sulfur or a sulfur containing compound such as hydrogen sulfide,
sulfur monohalide or sulfur dihalide, to form products which are generally mixtures
of compounds in which 2 or more phenols are bridged by sulfur containing bridges.
[0015] Carboxylate detergents, e.g., salicylates, can be prepared by reacting an aromatic
carboxylic acid with an appropriate metal compound such as an oxide or hydroxide and
neutral or overbased products may be obtained by methods well known in the art. The
aromatic moiety of the aromatic carboxylic acid can contain heteroatoms, such as nitrogen
and oxygen. Preferably, the moiety contains only carbon atoms; more preferably the
moiety contains six or more carbon atoms; for example benzene is a preferred moiety.
The aromatic carboxylic acid may contain one or more aromatic moieties, such as one
or more benzene rings, either fused or connected via alkylene bridges. The carboxylic
moiety may be attached directly or indirectly to the aromatic moiety. Preferably the
carboxylic acid group is attached directly to a carbon atom on the aromatic moiety,
such as a carbon atom on the benzene ring. More preferably, the aromatic moiety also
contains a second functional group, such as a hydroxy group or a sulfonate group,
which can be attached directly or indirectly to a carbon atom on the aromatic moiety.
[0016] Preferred examples of aromatic carboxylic acids are salicylic acids and sulfurized
derivatives thereof, such as hydrocarbyl substituted salicylic acid and derivatives
thereof. Processes for sulfurizing, for example a hydrocarbyl - substituted salicylic
acid, are known to those skilled in the art. Salicylic acids are typically prepared
by carboxylation, for example, by the Kolbe - Schmitt process, of phenoxides, and
in that case, will generally be obtained, normally in a diluent, in admixture with
uncarboxylated phenol.
[0017] Preferred substituents in oil - soluble salicylic acids are alkyl substituents. In
alkyl - substituted salicylic acids, the alkyl groups advantageously contain 5 to
100, preferably 9 to 30, especially 14 to 20, carbon atoms. Where there is more than
one alkyl group, the average number of carbon atoms in all of the alkyl groups is
preferably at least 9 to ensure adequate oil solubility.
[0018] Detergents generally useful in the formulation of lubricating oil compositions also
include "hybrid" detergents formed with mixed surfactant systems, e.g., phenate/salicylates,
sulfonate/phenates, sulfonate/salicylates, and sulfonate/phenate/salicylates, as described,
for example, in pending U.S. Patent Application Nos. 09/180,435 and 09/180,436 and
U.S. Patent Nos. 6,153,565 and 6,281,179.
[0019] Interaction with organic friction modifiers in lubricating additive concentrates
is particularly severe when the metal of the metal complex is calcium. Further, the
interaction with the organic friction modifier is more pronounced in concentrates
containing sulfonate detergents and complex detergents containing sulfonate surfactant.
Therefore, in a preferred embodiment, the basic metal complex is calcium overbased
detergent or overbased sulfonate or sulfonate-containing complex detergent, more preferably
overbased calcium sulfonate or sulfonate-containing complex detergent.
[0020] Oil-soluble hydrocarbyl phenol aldehyde condensates useful in the practice of the
present invention are those having the following structure:

wherein n is 0 to 10, preferably 1 to 8, more preferably 2 to 7, and most preferably
3 to 6; Y is a divalent bridging group, and is preferably a hydrocarbyl group, preferably
having from 1 to 4 carbon atoms; and R is a hydrocarbyl group having from 4 to 30,
preferably 8 to 18, and most preferably 9 to 15 carbon atoms.
[0021] The hydrocarbyl phenol aldehyde condensate is preferably a hydrocarbyl phenol formaldehyde
condensate. The term "hydrocarbyl" as used herein means that the group concerned is
primarily composed of hydrogen and carbon atoms and is bonded to the remainder of
the molecule via a carbon atom, but does not exclude the presence of other atoms or
groups in a proportion insufficient to detract from the substantially hydrocarbon
characteristics of the group. The hydrocarbyl group is preferably composed of only
hydrogen and carbon atoms. Advantageously, the hydrocarbyl group is an aliphatic group,
preferably alkyl or alkylene group, especially alkyl groups, which may be linear or
branched. R is preferably an alkyl or alkylene group. R is preferably branched.
[0022] The hydrocarbyl phenol aldehyde condensate preferably has a weight average molecular
weight (Mw) in the range of 600 to 4000, preferably 800 to 3500, more preferably 1000
to 2000, even more preferably 1200 to 1900, and most preferably 1400 to 1750, as measured
by MALDI-TOF (Matrix Assisted Laser Desorption Ionization- Time of Flight) Mass Spectrometry.
[0023] The hydrocarbyl phenol aldehyde condensate is preferably one obtained by a condensation
reaction between at least one aldehyde or ketone or reactive equivalent thereof and
at least one hydrocarbyl phenol, in the presence of an acid catalyst such as, for
example, an alkyl benzene sulphonic acid. The product is preferably subjected to stripping
to remove any unreacted hydrocarbyl phenol, preferably to less than 5 mass %, more
preferably to less than 3 mass %, even more preferably to less than 1 mass %, of unreacted
hydrocarbyl phenol. Most preferably, the product includes less than 0.5 mass %, such
as, for example, less than 0.1 mass % of unreacted hydrocarbyl phenol.
[0024] Although a basic catalyst can be used, an acid catalyst is preferred. The acid catalyst
may be selected from a wide variety of acidic compounds such as, for example, phosphoric
acid, sulphuric acid, sulphonic acid, oxalic acid and hydrochloric acid. The acid
may also be present as a component of a solid material such as acid treated clay.
The amount of catalyst used may vary from 0.05 to 10 mass % or more, such as for example
0.1 to 1 mass % of the total reaction mixture.
[0025] In particular, the hydrocarbyl phenol aldehyde condensate is preferably branched
dodecyl phenol formaldehyde condensate, such as, for example, a tetrapropenyl tetramer
phenol formaldehyde condensate.
[0026] The hydrocarbyl phenol aldehyde condensate is preferably present in the additive
concentrate in an amount ranging from about 2 to 20 mass %, preferably from about
5 to 15 mass %, and more preferably from about 10 to 12 mass %, based on the mass
of the concentrate.
[0027] Preferably, the organic friction modifier and hydrocarbyl phenol aldehyde condensate
are present in amounts providing a ratio of mass % organic friction modifier to mass
% hydrocarbyl phenol aldehyde condensate of from about 1:3 to about 1:7, more preferably
from about 1:1.5 to about 1:3.5, most preferably from about 1:1 to about 1:2.5. Thus,
a concentrate containing at least 3 mass % of the organic friction modifier preferably
contains at a minimum of from about 9 to about 21 mass % of hydrocarbyl phenol aldehyde
condensate.
[0028] Some, hydrocarbyl phenol aldehyde condensates are known to provide antioxidancy,
and dispersancy (see, for example, U.S. Patent No. 5,259,967 to Ripple). Therefore,
when a hydrocarbyl phenol aldehyde condensate is used to stabilize the additive package,
phenolic and/or aminic antioxidants commonly used to provide lubricating oil compositions
with oxidation inhibition could possibly be used in reduced amounts, or even eliminated.
Some hydrocarbyl phenol aldehyde condensates have also been found to provide inherent
detergency and when a hydrocarbyl phenol aldehyde condensate is used to stabilize
the additive package, the amount of metal detergent could possibly be reduced. Because
the hydrocarbyl phenol aldehyde condensates are free of metal and can also be free
of sulfur, any inherent detergency provides the compositions of the present invention
with an additional important advantage, particularly when the additive packages are
to be used for the formulation of the new generations of "Low SAPS" (Sulphated Ash,
Phosphorus and Sulphur) lubricants.
[0029] To provide additive package stability in the presence of 3 mass % or more of the
organic friction modifier, the hydrocarbyl phenol aldehyde condensate can be used
in an amount providing a ratio of mass % basic metal complex to mass % hydrocarbyl
phenol aldehyde condensate of from about 1:7 to about 23:1, preferably at least about
1:3 to about 6:1, more preferably from about 1:2 about 5:1.
[0030] In order for the concentrate to be oleaginous, the additives may be in solution in
an oleaginous carrier or such a carrier may be provided separately or both. Examples
of suitable carriers are oils of lubricating viscosity, such as described in detail
hereinafter, and aliphatic, naphthenic and aromatic hydrocarbons.
[0031] The oil of lubricating viscosity, useful for making concentrates of the invention,
or for making lubricating oil compositions from such concentrates, may be selected
from natural (vegetable, animal or mineral) and synthetic lubricating oils and mixtures
thereof. It may range in viscosity from light distillate mineral oils to heavy lubricating
oils such as gas engine oil, mineral lubricating oil, motor vehicle oil, and heavy
duty diesel oil. Generally, the viscosity of the oil ranges from 2 centistokes to
30 centistokes, especially 5 centistokes to 20 centistokes, at 100°C.
[0032] Natural oils include animal oils and vegetable oils (e.g., castor oil, lard oil);
liquid petroleum oils and hydro-refined, solvent-treated or acid-treated mineral oils
of the paraffinic, naphthenic and mixed paraffinic-naphthenic types. Oils of lubricating
viscosity derived from coal or shale also serve as useful base oils.
[0033] Synthetic lubricating oils include hydrocarbon oils and halo-substituted hydrocarbon
oils such as polymerized and interpolymerized olefms (e.g., polybutylenes, polypropylenes,
propylene-isobutylene copolymers, chlorinated polybutylenes, poly(1-hexenes), poly(1-octenes),
poly(1-decenes)); alkylbenzenes (e.g., dodecylbenzenes, tetradecylbenzenes, dinonylbenzenes,
di(2-ethylhexyl)benzenes); polyphenyls (e.g., biphenyls, terphenyls, alkylated polyphenols);
and alkylated diphenyl ethers and alkylated diphenyl sulfides and derivative, analogs
and homologs thereof.
[0034] Alkylene oxide polymers and interpolymers and derivatives thereof where the terminal
hydroxyl groups have been modified by esterification, etherification, etc., constitute
another class of known synthetic lubricating oils. These are exemplified by polyoxyalkylene
polymers prepared by polymerization of ethylene oxide or propylene oxide, and the
alkyl and aryl ethers of polyoxyalkylene polymers (e.g., methyl-polyiso-propylene
glycol ether having a molecular weight of 1000 or diphenyl ether of poly-ethylene
glycol having a molecular weight of 1000 to 1500); and mono- and polycarboxylic esters
thereof, for example, the acetic acid esters, mixed C
3-C
8 fatty acid esters and C
13 Oxo acid diester of tetraethylene glycol.
[0035] 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, sebasic acid, fumaric acid, adipic
acid, linoleic acid dimer, malonic acid, alkylmalonic acids, alkenyl malonic acids)
with a variety of alcohols (e.g., butyl alcohol, hexyl alcohol, dodecyl alcohol, 2-ethylhexyl
alcohol, ethylene glycol, diethylene glycol monoether, propylene glycol). Examples
of such esters include dibutyl adipate, di(2-ethylhexyl) sebacate, di-n-hexyl fumarate,
dioctyl sebacate, diisooctyl azelate, diisodecyl azelate, dioctyl phthalate, 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-ethylhexanoic acid.
[0036] Esters useful as synthetic oils also include those made from C
5 to C
12 monocarboxylic acids and polyols and polyol esters such as neopentyl glycol, trimethylolpropane,
pentaerythritol, dipentaerythritol and tripentaerythritol.
[0037] Silicon-based oils such as the polyalkyl-, polyaryl-, polyalkoxy- or polyaryloxysilicone
oils and silicate oils comprise another useful class of synthetic lubricants; such
oils include tetraethyl silicate, tetraisopropyl silicate, tetra-(2-ethylhexyl)silicate,
tetra-(4-methyl-2-ethylhexyl)silicate, tetra-(p-tert-butyl-phenyl) silicate, hexa-(4-methyl-2-ethylhexyl)disiloxane,
poly(methyl)siloxanes and poly(methylphenyl)siloxanes. Other synthetic lubricating
oils include liquid esters of phosphorous-containing acids (e.g., tricresyl phosphate,
trioctyl phosphate, diethyl ester of decylphosphonic acid) and polymeric tetrahydrofurans.
[0038] The oil of lubricating viscosity may comprise a Group I, Group II, Group III, Group
IV or Group V oil or blends of the aforementioned oils. The oil of lubricating viscosity
may also comprise a blend of a Group I oil and one or more of Group II, Group III,
Group IV or Group V oil.
[0039] Definitions for the oils as used herein are the same as those found in the American
Petroleum Institute (API) publication "Engine Oil Licensing and Certification System",
Industry Services Department, Fourteenth Edition, December 1996, Addendum 1, December
1998. Said publication categorizes oils as follows:
a) Group I oils contain less than 90 percent saturates and/or greater than 0.03 percent
sulfur and have a viscosity index greater than or equal to 80 and less than 120 using
the test methods specified in Table 1.
b) Group II oils contain greater than or equal to 90 percent saturates and less than
or equal to 0.03 percent sulfur and have a viscosity index greater than or equal to
80 and less than 120 using the test methods specified in Table 1. Although not a separate
Group recognized by the API, Group II oils having a viscosity index greater than about
110 are often referred to as "Group II+" oils.
c) Group III oils contain greater than or equal to 90 percent saturates and less than
or equal to 0.03 percent sulfur and have a viscosity index greater than or equal to
120 using the test methods specified in Table 1.
d) Group IV oils are polyalphaolefins (PAO).
e) Group V oils are all other base stocks not included in Group I, II, III, or IV.
Table 1
Property |
Test Method |
Saturates |
ASTM D2007 |
Viscosity Index |
ASTM D2270 |
Sulfur |
ASTM D4294 |
[0040] The oil of lubricating viscosity preferably has a saturate content of at least 65%,
more preferably at least 75%, such as at least 85%. Most preferably, the oil of lubricating
viscosity has a saturate content of greater than 90%. Preferably, the oil of lubricating
viscosity has a sulfur content of less than 1%, preferably less than 0.6%, more preferably
less than 0.3%, by mass, such as 0 to 0.3% by mass.
[0041] Preferably the volatility of the oil of lubricating viscosity, as measured by the
Noack test (ASTM D5880), is less than or equal to about 40 mass %, such as less than
or equal to about 35 mass %, preferably less than or equal to about 32 mass %, such
as less than or equal to about 28 mass %, more preferably less than or equal to about
16 mass %. Preferably, the viscosity index (VI) of the oil of lubricating viscosity
is at least 85, preferably at least 100, most preferably from about 105 to 140.
[0042] In addition to the overbased metal detergent, organic friction modifier and hydrocarbyl
phenol aldehyde condensate, a concentrate of the present invention, and fully formulated
lubricants formed therefrom, can contain a number of other performance improving additives
selected from ashless dispersants, antiwear agents, oxidation inhibitors or antioxidants,
metal-containing friction modifiers and fuel economy agents, antifoamants, corrosion
inhibitors, and polyalkenyl acylating agent. Conventionally, when formulating a lubricant,
the additives will be provided to the formulator in one or more, preferably a single
concentrated additive package, oftentimes referred to as a DI (dispersant-inhibitor)
package and a VI improver and/or VI improver and LOFI, will be provided in a second
package.
[0043] Ashless dispersants maintain in suspension oil insolubles resulting from oxidation
of the oil during wear or combustion. They are particularly advantageous for preventing
the precipitation of sludge and the formation of varnish, particularly in gasoline
engines.
[0044] Dihydrocarbyl dithiophosphate metal salts are frequently used as antiwear and antioxidant
agents. The metal may be an alkali or alkaline earth metal, or aluminum, lead, tin,
molybdenum, manganese, nickel or copper. The zinc salts are most commonly used in
lubricating oil and may be prepared in accordance with known techniques by first forming
a dihydrocarbyl dithiophosphoric acid (DDPA), usually by reaction of one or more alcohol
or a phenol with P
2S
5 and then neutralizing the formed DDPA with a zinc compound. For example, a dithiophosphoric
acid may be made by reacting mixtures of primary and secondary alcohols. Alternatively,
multiple dithiophosphoric acids can be prepared where the hydrocarbyl groups on one
are entirely secondary in character and the hydrocarbyl groups on the others are entirely
primary in character. To make the zinc salt, any basic or neutral zinc compound could
be used but the oxides, hydroxides and carbonates are most generally employed. Commercial
additives frequently contain an excess of zinc due to the use of an excess of the
basic zinc compound in the neutralization reaction.
[0045] Oxidation inhibitors or antioxidants reduce the tendency of mineral oils to deteriorate
in service. Oxidative deterioration can be evidenced by sludge in the lubricant, varnish-like
deposits on the metal surfaces, and by viscosity growth. Such oxidation inhibitors
include hindered phenols, alkaline earth metal salts of alkylphenolthioesters having
preferably C
5 to C
12 alkyl side chains, calcium nonylphenol sulfide, oil soluble phenates and sulfurized
phenates, phosphosulfurized or sulfurized hydrocarbons, phosphorous esters, metal
thiocarbamates, oil soluble copper compounds as described in U.S. Patent No. 4,867,890,
and molybdenum- containing compounds and aromatic amines.
[0046] Known metal-containing friction modifiers include oil-soluble organo-molybdenum compounds.
Such organo-molybdenum friction modifiers also provide antioxidant and antiwear credits
to a lubricating oil composition. As an example of such oil soluble organo-molybdenum
compounds, there may be mentioned the dithiocarbamates, dithiophosphates, dithiophosphinates,
xanthates, thioxanthates, sulfides, and the like, and mixtures thereof. Particularly
preferred are molybdenum dithiocarbamates, dialkyldithiophosphates, alkyl xanthates
and alkylthioxanthates.
[0047] Foam control can be provided by an antifoamant of the polysiloxane type, for example,
silicone oil or polydimethyl siloxane.
[0048] Some of the above-mentioned additives can provide a multiplicity of effects; thus
for example, a single additive may act as a dispersant-oxidation inhibitor. This approach
is well known and need not be further elaborated herein.
[0049] Representative effective amounts of such additional additives, when used in fully
formulated crankcase lubricants, are listed below in Table 2:
Table 2
ADDITIVE |
Mass % (Broad) |
Mass % (Preferred) |
Ashless Dispersant |
0.1 - 20 |
1 - 8 |
Metal Detergents |
0.1 - 15 |
0.2 - 9 |
Corrosion Inhibitor |
0 - 5 |
0 - 1.5 |
Metal Dihydrocarbyl Dithiophosphate |
0.1 - 6 |
0.1 - 4 |
Antioxidant |
0 - 5 |
0.01 - 2 |
Pour Point Depressant |
0.01 - 5 |
0.01 - 1.5 |
Antifoaming Agent |
0 - 5 |
0.001 - 0.15 |
Supplemental Antiwear Agents |
0 - 1.0 |
0 - 0.5 |
Friction Modifier |
0 - 5 |
0 - 1.5 |
Basestock |
Balance |
Balance |
[0050] The concentrates of the invention are preferably prepared at an elevated temperature,
i.e. above ambient temperature. Such concentrates may be prepared at a temperature
of at least 50°C such as at least 80°C, preferably at least 90°C, more preferably
at least 100°C. Although energy is saved at low temperatures, practical considerations
dictate the most convenient temperature that can be used. Thus, where an additive
is used that is solid at ambient temperature it is usually more convenient to raise
the temperature to a temperature at which the additive flows, rather than dissolving
it in oil prior to addition to the other additives. Temperatures of 100°C or more
can be employed if any additive is more conveniently handled at such temperatures.
Consideration must be given to the time for which it is held at the mixing temperature
and its stability under such temperatures and time conditions.
[0051] Conventionally, when forming additive concentrates, the dispersant and detergent
are pre-blended at a relatively high temperature, and the resulting pre-blend is then
mixed with the remaining additives at a lower temperature. The blending sequence has
not been found to have a significant impact on the effect of the hydrocarbyl phenol
aldehyde condensate on concentrate stability. Therefore, the hydrocarbyl phenol aldehyde
condensate can be pre-blended with the dispersant and detergent before being mixed
with the remaining additives, including the organic friction modifier, may be mixed
with other additives, including the organic friction modifier prior to contact with
the dispersant/detergent pre-blend, or can be introduced into the concentrate, as
a separate component at any stage during concentrate formation. The components of
the concentrate are advantageously held at the mixing temperature for a time sufficient
to achieve a homogenous mixture thereof. This can usually be accomplished within one
half hour, particularly when the temperature of mixing exceeds 80°C.
[0052] The concentrates of the invention can be incorporated into a lubricating oil composition
in any convenient way. Thus, they can be added directly to an oil of lubricating viscosity
by dispersing or dissolving them in the oil at the desired concentrations of the dispersant
and detergent, respectively. Such blending can occur at ambient temperature or elevated
temperatures. Alternatively, the composite can be blended with a suitable oil-soluble
solvent and base oil to form a further concentrate which is then blended with an oil
of lubricating viscosity to obtain the final lubricating oil composition. Such concentrate
will typically contain (on an active ingredient (A.I.) basis) from about 1.7 to about
20 mass %, preferably from about, preferably from about 3 to about 10 mass %, of the
organic friction modifier containing at least one hydroxyl or amino group, and from
about 3 to about 45 mass %, preferably from about 5 to about 30 mass %, more preferably
from about 7.5 to about 25 mass % of the basic metal complex, and from about 1 to
about 15 mass %, preferably from about 3 to about 13 mass %, more preferably from
about 6 to about 8 mass % of the hydrocarbyl phenol aldehyde condensate, based on
the total concentrate weight; the remainder of the concentrate comprising diluent
(preferably no more than about 90 mass %, such as not more than 80 mass %) oil and,
optionally, other additives.
[0053] This invention will be further understood by reference to the following examples,
wherein all parts are parts by weight (AI), unless otherwise noted and which include
preferred embodiments of the invention.
EXAMPLES
Synthesis Example A
[0054] Nonylphenol (10.5 mol) diluted in heptane was reacted with formaldehyde (9.0 mol)
in water using a sulphonic acid catalyst. The reagents were charged to a 5 L flask
and heated under nitrogen to 100°C. After addition of diluent oil, the water and heptane
were distilled off until the temperature reached 150°C. The reaction mixture was then
stripped under vacuum to remove residual solvent and yield a final product. The quantities
of the reagents used are provided in Table 3.
Table 3
Reagent |
Mass (g) |
nonylphenol |
2645 |
Paraformaldehyde |
270.3 |
Water |
661.7 |
Heptane |
1000 |
Sulfonic Acid Catalyst |
27.1 g |
Total Reagent |
4604 |
Diluent Oil |
1355.8 g |
[0055] The final product had a number average molecular weight (Mn) of about 840, a weight
average molecular weight (Mw) of about 1260 and contained about 0.09 mass % residual
nonylphenol, as determined by GPC and HPLC analysis.
Comparative Example 1
[0056] Conventional additive concentrates containing a 300 TBN calcium sulfonate detergent,
a C
8 hindered phenol antioxidant (Irganox L135, trade name, a product of Ciba Specialty
Chemicals Corporation) other conventional additives (dispersant, ZDDP, aminic antioxidant,
molybdenum based antiwear agent, antifoamant), diluent oil and increasing amounts
of organic friction modifiers (ethoxylated tallow amine (ETA) and glycerol monooleate
(GMO)), were prepared as shown in Table 4 (amounts expressed in terms of mass %).
Table 4
Component |
C1 |
C2 |
C3 |
C4 |
C5 |
Ca Sulf Det. |
17.8 |
17.8 |
17.8 |
17.8 |
17.8 |
Irganox L135 |
8.9 |
8.9 |
8.9 |
8.9 |
8.9 |
GMO |
0.0 |
1.1 |
1.7 |
2.2 |
3.3 |
ETA |
1.7 |
1.7 |
1.7 |
1.7 |
1.7 |
Other Additives |
54.9 |
54.9 |
54.9 |
54.9 |
54.9 |
Diluent |
16.8 |
15.7 |
15.1 |
14.5 |
13.4 |
Total |
100.0 |
100.0 |
100.0 |
100.0 |
100.0 |
Inventive Example 1
[0057] Additive concentrates of the present invention, in which the methylene bridged alkyl
phenol (MBAP) of Synthesis Example A was substituted for the Irganox L135 hindered
phenol antioxidant were then prepared as shown in Table 5 (amounts are expressed in
terms of mass %). The blending procedure and order were identical (preblending of
dispersant and detergent at higher temperature, followed by mixing of detergent/dispersant
preblend with other additives at lower temperature), to those used to form the concentrates
of Comparative Example 1.
Table 5
Component |
I1 |
I2 |
I3 |
I4 |
I5 |
I6 |
Ca Sulf Det. |
17.8 |
17.8 |
17.8 |
17.8 |
17.8 |
17.8 |
Irganox L135 |
0.0 |
0.0 |
0.0 |
0.0 |
0.0 |
0.0 |
MBAP |
5.6 |
5.6 |
5.6 |
11.1 |
11.1 |
11.1 |
GMO |
0.0 |
1.7 |
3.3 |
0.0 |
1.7 |
3.3 |
ETA |
1.7 |
1.7 |
1.7 |
1.7 |
1.7 |
1.7 |
Other Additives |
54.9 |
54.9 |
54.9 |
54.9 |
54.9 |
54.9 |
Diluent |
20.1 |
18.4 |
16.8 |
14.5 |
12.9 |
11.2 |
Total |
100.0 |
100.0 |
100.0 |
100.0 |
100.0 |
100.0 |
[0058] Each of the above additive concentrates was then subjected to a storage stability
test in which the concentrates were stored for a number of weeks at 60°C with periodic
measuring of the amount of sediment formed. A concentrate package failed the stability
test at the time the amount of sediment measured was greater than 0.05 vol. %, based
on the total weight of the concentrate. The results for the concentrates of Comparative
Example 1, containing the phenolic antioxidant are provided in Table 6. The results
achieved with the concentrates of Inventive Example 1 are provided in Table 7.
Table 6
Conc. ID |
C1 |
C2 |
C3 |
C4 |
C5 |
Week # |
|
|
|
|
|
1 |
Pass |
Pass |
Pass |
Pass |
Pass |
2 |
Pass |
Pass |
Pass |
Pass |
Pass |
3 |
Pass |
Pass |
Pass |
Pass |
Pass |
4 |
Pass |
Pass |
Pass |
Fail |
Fail |
5 |
Pass |
Pass |
Fail |
|
|
6 |
Pass |
Pass |
|
|
|
7 |
Pass |
Fail |
|
|
|
8 |
Pass |
|
|
|
|
Table 7
Conc.ID |
I1 |
I2 |
I3 |
I4 |
I5 |
I6 |
Week # |
|
|
|
|
|
|
1 |
Pass |
Pass |
Pass |
Pass |
Pass |
Pass |
2 |
Pass |
Pass |
Pass |
Pass |
Pass |
Pass |
3 |
Pass |
Pass |
Pass |
Pass |
Pass |
Pass |
4 |
Pass |
Pass |
Pass |
Pass |
Pass |
Pass |
5 |
Pass |
Pass |
Pass |
Pass |
Pass |
Pass |
6 |
Pass |
Pass |
Fail |
Pass |
Pass |
Pass |
7 |
Pass |
Pass |
|
Pass |
Pass |
Fail |
8 |
Pass |
Pass |
|
Pass |
Pass |
|
[0059] As shown by the foregoing, in the concentrates containing 8.89 mass % of the phenolic
antioxidant, the presence of 3.34 mass % total of organic friction modifier caused
formation of an unacceptable level of sediment after only four weeks of storage. As
the total amount of organic friction modifier increased to 3.88 mass % and 5 mass
%, failure of the storage stability test occurred at only 5 weeks and 4 weeks, respectively.
In contrast, in the presence of only 5.56 mass % of MBAP, concentrates containing
a total of 3.34 mass % of organic friction modifier remained stable at the end of
the eight week stability test, and the concentrate containing a total of 5 mass %
of organic friction modifier remained stable for six weeks. Increasing the amount
of MBAP to 11.11 mass % allowed concentrates containing a total of 5 mass % of organic
friction modifier to remain stable through the end of the seventh week.
[0060] The disclosures of all patents, articles and other materials described herein are
hereby incorporated, in their entirety, into this specification by reference. A description
of a composition comprising, consisting of, or consisting essentially of multiple
specified components, as presented herein and in the appended claims, should be construed
to also encompass compositions made by admixing said multiple specified components.
The principles, preferred embodiments and modes of operation of the present invention
have been described in the foregoing specification. What applicants submit is their
invention, however, is not to be construed as limited to the particular embodiments
disclosed, since the disclosed embodiments are regarded as illustrative rather than
limiting.
1. A lubricating oil additive concentrate comprising an oil of lubricating viscosity,
a basic metal complex, an oil-soluble hydrocarbyl phenol aldehyde condensate, and
at least 1.7 mass %, based on the total mass of said concentrate, of an organic friction
modifier containing at least one hydroxyl or amino group.
2. A lubricating oil additive concentrate according to claim 1, wherein said oil-soluble
hydrocarbyl phenol aldehyde condensate is at least one compound of the formula:

wherein n is 0 to 10; Y is a divalent bridging group; and R is a hydrocarbyl group
having from 4 to 30 carbon atoms.
3. A concentrate according to claim 2, wherein n is 3 to 6; Y is a hydrocarbyl group
having from 1 to 4 carbon atoms; and R is a hydrocarbyl group having from 9 to 15
carbon atoms.
4. A concentrate according to claim 1, 2 or 3, comprising from about 2 mass % to about
20 mass % of said oil-soluble hydrocarbyl phenol aldehyde condensate, based on the
total mass of said concentrate.
5. A concentrate according to in claim 4, comprising from about 10 mass % to about 12
mass % of said oil-soluble hydrocarbyl phenol aldehyde condensate, based on the total
mass of said concentrate.
6. A concentrate according to any one of the preceding claims, wherein said organic friction
modifier is selected from the group consisting of glycerol esters of higher fatty
acids; esters of long chain polycarboxylic acids with diols; oxazoline compounds;
alkoxylated alkyl-substituted mono-amines, diamines and alkyl ether amines; and mixtures
thereof.
7. A concentrate according to claim 6, wherein said organic friction modifier is selected
from the group consisting of glycerol oleates; ethoxylated amines; and mixtures thereof.
8. A concentrate according to any one of the preceding claims, comprising at least 3
mass %, preferably at least 5 mass % of said organic friction modifier, based on the
total mass of said concentrate.
9. A concentrate according to any one of the preceding claims, wherein said basic metal
complex is an overbased metal detergent.
10. A concentrate according to claim 9, wherein said overbased metal detergent is selected
from the group consisting of overbased calcium sulfonates, overbased magnesium sulfonates,
overbased calcium phenates, overbased magnesium phenates, overbased calcium carboxylates,
overbased magnesium carboxylates, overbased calcium hybrid detergents containing surfactant
systems comprising at least two of sulfonate, phenate and carboxylate surfactant,
overbased magnesium hybrid detergents containing surfactant systems comprising at
least two of sulfonate, phenate and carboxylate surfactant, and mixtures thereof.
11. A concentrate according to claim 10, wherein said overbased metal detergent is an
overbased calcium detergent.
12. A concentrate according to claim 10 or 11, wherein said overbased metal detergent
is an overbased metal sulfonate detergent, or an overbased metal hybrid detergent
containing a surfactant system comprising sulfonate surfactant and at least one other
surfactant.
13. A concentrate according to claim 10, wherein said overbased metal detergent is an
overbased calcium sulfonate detergent, or an overbased calcium hybrid detergent containing
a surfactant system comprising sulfonate surfactant and at least one other surfactant.
14. A concentrate according to any one of the preceding claims, wherein said organic friction
modifier and said hydrocarbyl phenol aldehyde condensate are present in amounts providing
a ratio of mass % organic friction modifier to mass % hydrocarbyl phenol aldehyde
condensate of from about 1:3 to about 1:7.
15. A concentrate according to any one of the preceding claims, wherein said basic metal
complex and said hydrocarbyl phenol aldehyde condensate are present in amounts providing
a ratio of mass % basic metal complex to mass % hydrocarbyl phenol aldehyde condensate
of from about 1:7 to about 23:1.
16. A concentrate according to any one of the preceding claims, comprising at least about
3 mass % of said organic friction modifier and at least from about 9 mass % to at
least about 21 mass % of said hydrocarbyl phenol aldehyde condensate.
17. A concentrate according to claim 16, further comprising from about 3 to about 45 mass
% of said basic metal complex.
18. A concentrate according to any one of the preceding claims, further comprising at
least one other additive selected from the group consisting of dispersant, antioxidants
and antiwear agents.
19. A method of improving the stability of a lubricant additive concentrate comprising
an admixture of a basic metal complex and an organic friction modifier having at least
one hydroxyl or amino group, which method comprises introducing into said concentrate
an oil-soluble hydrocarbyl phenol aldehyde condensate.
20. A method according to claim 19, wherein the additive concentrate comprises at least
1.7 mass % of a organic friction modifier, at least 5 wt. % of an overbased metal
detergent, and no more than 90 wt. % of oil of lubricating viscosity.
21. Use of an oil-soluble hydrocarbyl phenol aldehyde condensate to stabalise a lubricant
additive concentrate comprising an admixture of a basic metal complex and at least
1.7 mass %, based on the total mass of the concentrate, of an organic friction modifier
having at least one hydroxyl or amino group.
22. The use according to claim 21, wherein the hydrocarbyl phenol aldehyde condensate
has the formula:

wherein n is 0 to 10; Y is a divalent bridging group; and R is a hydrocarbyl group
having from 4 to 30 carbon atoms.