[0001] The present invention relates to detergent additives for lubricating oil compositions.
[0002] Detergent additives are used in a wide variety of automotive, marine, railroad and
industrial lubricants to minimize high temperature engine varnish and lacquer deposits.
They are usually metal salts of sulphonates, phenates and salicylates, such as, for
examples, calcium sulphurized phenates. However, the use of sulphur-containing detergents
will soon be restricted due to imposed chemical limits on sulphur.
[0003] The aim of the present invention is to provide a detergent that is free of sulphur
and metal (i.e. ash).
[0004] In accordance with the present invention there is provided use as a detergent in
a lubricating oil composition of an oil-soluble hydrocarbyl phenol aldehyde condensate
having the following structure:

wherein n is 0 to 10, preferably 1 to 8, more preferably 2 to 6, and most preferably
3 to 5; 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; the oil-soluble hydrocarbyl
phenol aldehyde condensate having a weight average molecular weight (Mw) of 1250 to
1680, as measured by MALDI-TOF (Matrix Assisted Laser Desorption lonization- Time
of Flight) mass spectrometry.
[0005] The hydrocarbyl phenol aldehyde condensate has the advantage of being free of metals
(such as, for example, calcium and magnesium) and sulphur. Furthermore, unlike salicylate
detergents, the hydrocarbyl phenol aldehyde condensate does not exhibit negative interactions
with dispersants.
[0006] The hydrocarbyl phenol aldehyde condensate is preferably a hydrocarbyl phenol formaldehyde
condensate.
[0007] 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.
[0008] In accordance with the present invention there is also provided a method of improving
the detergency of a lubricating oil composition, the method including the step of
adding the hydrocarbyl phenol aldehyde condensate defined above to the lubricating
oil composition.
[0009] The hydrocarbyl phenol aldehyde condensate preferably has a weight average molecular
weight (Mw) in the range of 1280 to 1650, preferably 1300 to 1650, more preferably
1350 to 1600, as measured by MALDI-TOF (Matrix Assisted Laser Desorption lonization-
Time of Flight) Mass Spectrometry.
[0010] The hydrocarbyl phenol aldehyde condensate is preferably obtainable by the 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 5.0% mass, more
preferably to less than 3.0% mass, even more preferably to less than 1.0% mass, of
unreacted hydrocarbyl phenol. Most preferably, the product includes less than 0.5%,
such as, for example, less than 0.1 %, mass of unreacted hydrocarbyl phenol.
[0011] 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 an acid treated clay.
The amount of catalyst used may vary from 0.05 to 10% or more, such as for example
0.1 to 1 %, by mass of the total reaction mixture.
[0012] In particular, the hydrocarbyl phenol aldehyde condensate is preferably branched
dodecyl phenol formaldehyde condensate, such as, for example, a tetrapropenyl tetramer
phenol formaldehyde condensate.
[0013] The hydrocarbyl phenol aldehyde condensate is preferably used in the lubricating
oil composition in an amount ranging from 0.1 to 20 mass%, more preferably from 0.2
to 15 mass%, and most preferably from 0.3 to 10 mass%, based on the mass of the lubricating
oil composition.
Oil of Lubricating Viscosity
[0014] The lubricating oil composition will include an oil of lubricating viscosity. The
oil of lubricating viscosity (also referred to as lubricating oil) may be any oil
suitable for the lubrication of automotive, marine, railroad and industrial engines.
The lubricating oil may suitably be an animal, a vegetable or a mineral oil. Suitably
the lubricating oil is a petroleum-derived lubricating oil, such as a naphthenic base,
paraffinic base or mixed base oil. Alternatively, the lubricating oil may be a synthetic
lubricating oil. Suitable synthetic lubricating oils include synthetic ester lubricating
oils, which oils include diesters such as di-octyl adipate, di-octyl sebacate and
tridecyl adipate, or polymeric hydrocarbon lubricating oils such as, for example,
liquid polyisobutene and poly-alpha olefins. Commonly, a mineral oil is employed.
The lubricating oil generally comprises greater than 60, typically greater than 70,
mass% of the lubricant. The lubricating oil typically has a kinematic viscosity at
100°C of from 2 to 40, for example from 3 to 15, mm
2s
-1 and a viscosity index of from 80 to 100, for example, from 90 to 95.
[0015] Another class of lubricating oils is hydrocracked oils, where the refining process
further breaks down the middle and heavy distillate fractions in the presence of hydrogen
at high temperatures and moderate pressures. Hydrocracked oils typically have a kinematic
viscosity at 100°C of from 2 to 40, for example from 3 to 15, mm
2s
-1 and a viscosity index typically in the range of from 100 to 110, for example from
105 to 108.
[0016] The oil may include 'brightstock' which refers to base oils that are solvent-extracted,
de-asphalted products from vacuum residuum generally having a kinematic viscosity
at 100°C of from 28 to 36 mm
2s
-1 and are typically used in a proportion of less than 30, preferably less than 20,
more preferably less than 15, most preferably less than 10, such as less than 5, mass%,
based on the mass of the composition.
[0017] Most preferably, the oil of lubricating viscosity is present in the lubricating oil
composition in an amount greater than 50 mass%, more preferably greater than 60 mass%,
and most preferably greater than 65 mass%, based on the mass of the lubricating oil
composition.
Detergent Additives
[0018] The lubricating oil composition may also include one or more detergent additives
based on metal "soaps", that is metal salts of acidic organic compounds, sometimes
referred to as surfactants.
[0019] The metal may be an alkali or alkaline earth metal such as, for example, sodium,
potassium, lithium, calcium, barium and magnesium. Calcium is preferred.
[0020] The surfactant may be a salicylate, a sulphonate, a carboxylate, a phenate, a thiophosphate
or a naphthenate.
[0021] The detergent may also be a complex/hybrid detergent prepared from a mixture of more
than one metal surfactant, such as a calcium alkyl phenate and a calcium alkyl salicylate.
Such a complex detergent is a hybrid material in which the surfactant groups, for
example phenate and salicylate, are incorporated during the overbasing process. Examples
of complex detergents are described in the art, such as, for example, in EP 902 827B.
[0022] Surfactants for the surfactant system of the metal detergents contain at least one
hydrocarbyl group, for example, as a substituent on an aromatic ring.
[0023] The detergents may be non-sulphurized or sulph urized, and may be chemically modified
and/or contain additional substituents. Suitable sulphurizing processes are well known
to those skilled in the art.
[0024] The detergent may have a low TBN of from 10 to 50, a medium TBN of 50 to 150, or
a high TBN of greater than 150, such as, for example, 150 to 400.
[0025] The detergents may be used in a proportion in the range of 0.5 to 30, preferably
2 to 20, or more preferably 2 to 15, mass% based on the mass of the lubricating oil
composition.
Dispersant
[0026] The lubricant composition may include at least one dispersant. A dispersant is an
additive for a lubricating composition whose primary function in lubricants is to
accelerate neutralization of acids by the detergent system.
[0027] A noteworthy class of dispersants are "ashless", meaning a non-metallic organic material
that forms substantially no ash on combustion, in contrast to metal-containing, hence
ash-forming, materials. Ashless dispersants comprise a long chain hydrocarbon with
a polar head, the polarity being derived from inclusion of, e.g., an O, P or N atom.
The hydrocarbon is an oleophilic group that confers oil-solubility, having for example
40 to 500 carbon atoms. Thus, ashless dispersants may comprise an oil-soluble polymeric
hydrocarbon backbone having functional groups that are capable of associating with
particles to be dispersed.
[0028] Examples of ashless dispersants are succinimides, e.g. polyisobutene succinic anhydride;
and polyamine condensation products that may be borated or unborated.
[0029] The dispersants may be used in a proportion in the range of 0 to 10.0, preferably
0.5 to 6.0, or more preferably 1.0 to 4.0, mass% based on the mass of the lubricating
oil composition.
Antiwear Additives
[0030] Antiwear additives may be present in the lubricating oil composition. The antiwear
additives may be metallic or non-metallic, preferably the former.
[0031] Dihydrocarbyl dithiophosphate metal salts are examples of anti-wear additives that
may be used in the present invention. The metal in the dihydrocarbyl dithiophosphate
metal salts may be an alkali or alkaline earth metal, or aluminium, lead, tin, molybdenum,
manganese, nickel or copper. Zinc salts are preferred, preferably in the range of
0.1 to 1.5, preferably 0.5 to 1.3, mass%, based upon the total mass of the lubricating
oil composition. They may be prepared in accordance with known techniques by firstly
forming a dihydrocarbyl dithiophosphoric acid (DDPA), usually by reaction of one or
more alcohols 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 comprising both hydrocarbyl groups
that are entirely secondary and hydrocarbyl groups that are entirely primary. To make
the zinc salt, any basic or neutral zinc compound may be used but the oxides, hydroxides
and carbonates are most generally employed. Commercial additives frequently contain
an excess of zinc due to use of an excess of the basic zinc compound in the neutralization
reaction.
[0032] The preferred zinc dihydrocarbyl dithiophosphates are oil-soluble salts of dihydrocarbyl
dithiophosphoric acids and may be represented by the following formula:
[(RO) (R
1O) P(S)S]
2 Zn
where R and R
1 may be the same or different hydrocarbyl radicals containing from 1 to 18, preferably
2 to 12, carbon atoms and including radicals such as alkyl, alkenyl, aryl, arylalkyl,
alkaryl and cycloaliphatic radicals. Particularly preferred as R and R
1 groups are alkyl groups of 2 to 8 carbon atoms. Thus, the radicals may, for example,
be ethyl, n-propyl, l-propyl, n-butyl, l-butyl, sec-butyl, amyl, n-hexyl, l-hexyl,
n-octyl, decyl, dodecyl, octadecyl, 2-ethylhexyl, phenyl, butylphenyl, cyclohexyl,
methylcyclopentyl, propenyl, butenyl. In order to obtain oil-solubility, the total
number of carbon atoms (i.e. in R and R
1) in the dithiophoshoric acid will generally be 5 or greater. The zinc dihydrocarbyl
dithiophosphate can therefore comprise zinc dialkyl dithiophosphates.
[0033] The antiwear additive may be used in a proportion in the range of 0.1 to 1.5, preferably
0.2 to 1.3, or more preferably 0.5 to 0.9, mass% based on the mass of the lubricating
oil composition.
Antioxidants
[0034] Antioxidants may also be added to the lubricating oil composition. These may be aminic
or phenolic. Examples of aminic include secondary aromatic amines such as diarylamines,
for example diphenylamines wherein each phenyl group is alkylsubstituted with an alkyl
group having 4 to 15 carbon atoms. Examples of phenolics include hindered phenols,
including mono-phenols and bis-phenols. The anti-oxidant may be present in an amount
of up to 3 mass%.
[0035] One or more of the following additives may also be present in the lubricating oil
composition: pour point depressants such as poly(meth)acrylates or alkyl aromatic
polymers; anti-foaming agents such as silicone anti-foaming agents; viscosity index
improvers such as olefin copolymers; dyes; metal deactivators such as aryl thiazines,
triazoles or alkyl substituted dimercapto thiadiazoles; and demulsifiers.
[0036] It may be desirable to prepare an additive package or concentrate of the lubricating
oil composition. The additive package may be added simultaneously to the base oil
to form the lubricating oil composition Dissolution of the additive package into the
lubricating oil may be facilitated by solvents and by mixing accompanied with mild
heating. The additive package will typically be formulated to contain the detergent
in proper amounts to provide the desired concentration, and/or to carry out the intended
function in the final formulation when the additive package is combined with a predetermined
amount of base lubricant. The additive package may contain active ingredients in an
amount, based on the additive package, of, for example, from 2.5 to 90, preferably
from 5 to 75, most preferably from 8 to 60, mass% of additives in the appropriate
proportions, the remainder being base oil.
[0037] The final formulations may typically contain about 5 to 40 mass% of the additive
package, the remainder being base oil.
[0038] The terms 'oil-soluble' or 'oil-dispersable' as used herein do not necessarily indicate
that the compounds or additives are soluble, dissolvable, miscible or capable of being
suspended in the oil in all proportions. These do mean, however, that they are, for
instance, soluble or stably dispersible in oil to an extent sufficient to exert their
intended effect in the environment in which the oil is employed. Moreover, the additional
incorporation of other additives may also permit incorporation of higher levels of
a particular additive, if desired.
[0039] The invention will be further described, by way of example only, with reference to
the following examples:
Preparation of Hydrocarbyl Phenol Aldehyde Condensates
Reaction Components
[0040]
| |
Hydrocarbyl Phenol Aldehyde Condensates |
| 1100 Mw |
1300 Mw |
1500 Mw |
1585 Mw |
1700 Mw |
| Dodecylphenol |
2200 |
2200 |
2200 |
2200 |
2200 |
| Sulphonic Acid Catalyst |
22 |
22 |
22 |
22 |
22 |
| Paraformaldehyde |
165 |
182 |
197 |
204 |
213 |
| Water |
550 |
550 |
550 |
550 |
550 |
| Heptane |
831 |
831 |
831 |
831 |
831 |
[0041] In the Table above, the amounts are given in grams for the reaction components for
preparing hydrocarbyl phenol aldehyde condensates having weight average molecular
weights (Mw) ranging from 1100 to 1700.
Method
[0042] The dodecylphenol, sulphonic acid catalyst, paraformaldehyde, water and heptane were
added to a 5L baffled reactor with stirrer (200 rpm), nitrogen blanket (600ml/min),
condenser, Dean and Stark trap, a temperature controlling system, and Cardice/Acetone
trap vacuum system. The reaction components were heated from ambient to 80°C over
30 minutes, then heated further from 80 to 100°C over 2 hours, during which time water
was removed by azeotropic distillation. The residual heptane and dodecyl phenol were
removed from the reaction mixture under reduced pressure at 200°C. Finally, the temperature
was decreased to 120°C at which point ESN 150 was added to produce the desired level
of active ingredient (A.I.).
Example 1 and Comparative Example 1
[0043] Lubricating oil compositions were prepared and tested in the Caterpillar 1 N engine
test. Both compositions have the same ash and soap levels (i.e. 1% ash and 0.9% soap).
| |
Example 1 |
Comparative Example 1 |
| 300 TBN Calcium sulphonate |
1.81 |
1.26 |
| 400 TBN Magnesium Sulphonate |
0.26 |
0.26 |
| 147 TBN Calcium Sulphurized Phenate |
|
1.13 |
| Dodecylphenol Formaldehyde Condensate- 1585 mw |
0.45 |
0 |
| Succinimide Dispersant |
6.10 |
6.10 |
| ZDDP Antioxidant |
1.31 |
1.31 |
| Antioxidant |
0.26 |
0.26 |
| Seals Moderator |
0.17 |
0.17 |
| SN150 Diluent |
1.84 |
1.70 |
| Group I Base Oil,600N |
18.5 |
19.8 |
| Group I Base Oil, 150N |
61.3 |
60 |
| Viscosity Modifier |
7.8 |
7.8 |
| Pour Point Depressant |
0.2 |
0.2 |
| |
|
|
| Ash (%mass) |
1.00 |
1.00 |
| TBN (D2896) |
8.61 |
8.65 |
| Soap (%mass) |
0.91 |
0.91 |
| Sulphur (%mass) |
0.257 |
0.284 |
| Phosphorus (%mass) |
0.105 |
0.105 |
[0044] The Caterpillar 1 N engine test is designed to measure detergency. The test is made
up of three detergency measurements: the amount of carbon in the top piston groove
(top groove fill); the amount of heavy carbon on the top land of the piston (top land
heavy carbon); and the overall piston cleanliness, measured as weighted demerits (weighted
demerits, or WDN). The engine is sensitive to ash levels so both formulations were
formulated to have the same ash levels.
Caterpillar 1 N Engine Test Results
[0045]
| |
Caterpillar 1N Test Results |
| Example 1 |
Comparative Example 1 |
| Weighted Piston Demerits (WDN) |
178.5 |
272.1 |
| Top Groove Fill (TGF) |
8 |
38 |
| Top Land Heavy Carbon (TLHC) |
0 |
4 |
| Oil Consumption 0-252 hours (g/KW-h) |
0.11 |
0.13 |
| Ring Sticking |
none |
none |
[0046] Only example 1, which includes the dodecylphenol formaldehyde condensate, passes
all of the tests in the Caterpillar 1 N Test.
Example 2 and Comparative Example 2
[0047] Lubricating oil compositions were also prepared and tested in the Komatsu Hot Tube
Test.
| |
Example 2 |
Comparative Example 2 |
| 300 TBN Calcium Sulphonate |
1.45 |
1.45 |
| 400 TBN Magnesium Sulphonate |
0.30 |
0.30 |
| 147 TBN Calcium Sulphurized Phenate |
- |
1.30 |
| Succinimide Dispersant |
7.00 |
7.00 |
| ZDDP Antiwear |
1.60 |
1.60 |
| Antioxidant |
0.40 |
0.40 |
| Antifoam |
0.003 |
0.003 |
| PIBSA |
0.20 |
0.20 |
| Dodecylphenol Formaldehyde Condensate (stripped to <1% alkyl phenol) Mw 1500 |
1.08 |
- |
| SN 150 Diluent |
2.37 |
2.15 |
| Gp I Base Oil |
Balance |
Balance |
[0048] The results are shown below:
| |
Example 2 |
Comparative Example 2 |
| Visual Rating: 0 to 9 (0 = black and 9= clear) @ 280°C over 16 hours |
7 |
4 |
Effect of Weight Average Molecular Weight (Mw) on Performance of Hydrocarbyl Phenol
Aldehyde Condensate
[0049] The following formulations were tested to show the effect of weight average molecular
weight (Mw) of the hydrocarbyl phenol aldehyde condensates ('HPAC's) on performance
in the Caterpillar 1 N Test:
| |
Comparative 1100 Mw |
1300 Mw |
1500 Mw |
1585 Mw |
Comparative 1700 Mw |
| 300 TBN Calcium sulphonate |
1.81 |
1.81 |
1.81 |
1.81 |
1.81 |
| 400 TBN Magnesium Sulphonate |
0.26 |
0.26 |
0.26 |
0.26 |
0.26 |
| HPAC Mw 1100 |
0.45 |
|
|
|
|
| HPAC Mw 1300 |
|
0.45 |
|
|
|
| HPAC Mw 1500 |
|
|
0.45 |
|
|
| HPAC Mw 1585 |
|
|
|
0.45 |
|
| HPAC Mw 1700 |
|
|
|
|
0.45 |
| Succinimide Dispersant |
6.10 |
6.10 |
6.10 |
6.10 |
6.10 |
| ZDDP |
1.31 |
1.31 |
1.31 |
1.31 |
1.31 |
| Antioxidant |
0.26 |
0.26 |
0.26 |
0.26 |
0.26 |
| PIBSA |
0.17 |
0.17 |
0.17 |
0.17 |
0.17 |
| SN150 diluent |
1.70 |
1.70 |
1.70 |
1.70 |
1.70 |
| Gp I base oil |
Balance |
Balance |
Balance |
Balance |
Balance |
| |
|
|
|
|
|
| Ash (%) |
1.00 |
1.00 |
1.00 |
1.00 |
1.00 |
| TBN (ASTM D2896) |
8.61 |
8.61 |
8.61 |
8.61 |
8.61 |
| % Ca |
0.209 |
0.209 |
0.209 |
0.209 |
0.209 |
| % P |
0.105 |
0.105 |
0.105 |
0.105 |
0.105 |
| % S |
0.257 |
0.257 |
0.257 |
0.257 |
0.257 |
| Weighted Piston Demerits (WDN) |
229 |
218 |
170 |
179 |
266 |
| Top Groove Fill (TGF) |
62 |
15 |
12 |
8 |
25 |
[0050] As shown above, the hydrocarbyl phenol aldehyde condensates having weight average
molecular weights of 1300, 1500 and 1585 show surprisingly better performance in the
Caterpillar 1 N test than the hydrocarbyl phenol aldehyde condensates having weight
average molecular weights of 1100 and 1700.
1. A lubricating oil composition, comprising a major amount of an oil of lubricating
viscosity and a detergent composition comprising (A) an overbased metal salt of an
organic acid and (B) an oil-soluble hydrocarbyl phenol aldehyde condensate having
the following structure:

wherein n is 0 to 10, preferably 1 to 8, more preferably 2 to 6, and most preferably
3 to 5; 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; the oil-soluble hydrocarbyl
phenol aldehyde condensate having a weight average molecular weight (Mw) of 1250 to
1680, as measured by MALDI-TOF (Matrix Assisted Laser Desorption lonization- Time
of Flight) mass spectrometry.
2. A lubricating oil composition according to claim 1, wherein the hydrocarbyl phenol
aldehyde condensate has a number average molecular weight (Mw) in the range of 1280
to 1650, preferably 1300 to 1650, more preferably 1350 to 1600, as measured by MALDI-TOF
(Matrix Assisted Laser Desorption Ionization-Time of Flight) Mass Spectrometry.
3. A lubricating oil composition according to claim 1 or 2, wherein the condensate includes
less than 5.0% mass, more preferably less than 3.0% mass, even more preferably to
less than 1.0% by mass, of unreacted hydrocarbyl phenol.
4. A lubricating oil composition according to claim 1, 2 or 3, wherein hydrocarbyl phenol
aldehyde condensate is obtainable by the condensation reaction between at least one
aldehyde or ketone or reactive equivalent thereof and a hydrocarbyl phenol, in the
presence of an acid catalyst.
5. A lubricating oil composition according to any one of the preceding claims, wherein
the hydrocarbyl group in the hydrocarbyl phenol aldehyde condensate is branched.
6. A lubricating oil composition according to any one of the preceding claims, wherein
the hydrocarbyl phenol aldehyde condensate is a hydrocarbyl phenol formaldehyde condensate.
7. A lubricating oil composition according to any one of the preceding claims, wherein
the hydrocarbyl phenol aldehyde condensate is tetrapropenyl phenol formaldehyde condensate.
8. A lubricating oil composition according to any one of the preceding claims, wherein
the composition is a crankcase lubricating oil composition.
9. An additive concentrate for a lubricating oil composition comprising (A) an overbased
metal salt of an organic acid and (B) an oil-soluble hydrocarbyl phenol aldehyde condensate
having the following structure:

wherein n is 0 to 10, preferably 1 to 8, more preferably 2 to 6, and most preferably
3 to 5; 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; the oil-soluble hydrocarbyl
phenol aldehyde condensate having a weight average molecular weight (Mw) of 1250 to
1680, as measured by MALDI-TOF (Matrix Assisted Laser Desorption lonization- Time
of Flight) mass spectrometry.