U.S. patent application number 12/017385 was filed with the patent office on 2009-07-23 for lubricating oil composition.
Invention is credited to Nancy Z. Diggs, Thomas Joseph Mulrane, Robert Raymond Salgueiro.
Application Number | 20090186784 12/017385 |
Document ID | / |
Family ID | 40436422 |
Filed Date | 2009-07-23 |
United States Patent
Application |
20090186784 |
Kind Code |
A1 |
Diggs; Nancy Z. ; et
al. |
July 23, 2009 |
Lubricating Oil Composition
Abstract
SAE 0W and SAE 5W multigrade crankcase lubricating oil
compositions for heavy duty diesel (HDD) engines meeting the
performance requirements of at least one of the API CJ-4; API-CI-4,
and/or ACEA A7 specifications, having a sulfated ash content of no
greater than 1.0 mass %, a sulfur content of no greater than 0.4
mass %, and a phosphorus content of no greater than 0.12 mass %,
formulated with a major amount of oil of lubricating viscosity
including less than about 30 mass %, based on the total mass of oil
of lubricating viscosity, of Group IV and/or Group V base stock, at
least 0.3 mass %, of a non-hydrogenated olefin polymer; and greater
than about 40 ppm, of boron.
Inventors: |
Diggs; Nancy Z.; (Westfield,
NJ) ; Mulrane; Thomas Joseph; (Sandy Hook, CT)
; Salgueiro; Robert Raymond; (Roselle Park, NJ) |
Correspondence
Address: |
INFINEUM USA L.P.
P.O. BOX 710
LINDEN
NJ
07036
US
|
Family ID: |
40436422 |
Appl. No.: |
12/017385 |
Filed: |
January 22, 2008 |
Current U.S.
Class: |
508/155 |
Current CPC
Class: |
C10N 2030/42 20200501;
C10N 2030/44 20200501; C10N 2030/43 20200501; C10N 2030/06
20130101; C10N 2030/52 20200501; C10N 2010/04 20130101; C10M
2219/068 20130101; C10M 2205/026 20130101; C10N 2030/45 20200501;
C10M 2219/046 20130101; C10N 2020/04 20130101; C10M 2207/028
20130101; C10N 2060/14 20130101; C10M 167/00 20130101; C10M
2203/1025 20130101; C10M 2223/045 20130101; C10N 2040/252 20200501;
C10M 2203/1025 20130101; C10N 2020/02 20130101; C10M 2223/045
20130101; C10N 2010/04 20130101; C10M 2219/068 20130101; C10N
2010/12 20130101; C10M 2219/046 20130101; C10N 2010/04 20130101;
C10M 2207/028 20130101; C10N 2010/04 20130101; C10M 2219/068
20130101; C10N 2010/12 20130101; C10M 2223/045 20130101; C10N
2010/04 20130101; C10M 2219/046 20130101; C10N 2010/04 20130101;
C10M 2207/028 20130101; C10N 2010/04 20130101; C10M 2203/1025
20130101; C10N 2020/02 20130101 |
Class at
Publication: |
508/155 |
International
Class: |
C10M 125/26 20060101
C10M125/26; C10M 143/06 20060101 C10M143/06 |
Claims
1. An SAE 0W or 5W multigrade lubricating oil composition having a
sulfated ash content of no greater than 0.1 mass %, a sulfur
content of no greater than 0.4 mass %, and a phosphorus content of
no greater than 0.12 mass % and meeting the wear performance
requirements of at least one of API CJ-4; API CI-4; and ACEA E7,
said lubricating oil composition comprising: (a) a major amount of
oil of lubricating viscosity wherein said oil of lubricating
viscosity comprises no greater than about 30 mass % of one or more
Group IV base stock and/or Group V base stock; (b) at least about
0.3 mass % of a non-hydrogenated olefin polymer; and (c) at least
40 ppm of boron.
2. A lubricating oil composition, as claimed in claim 1, wherein
said oil of lubricating viscosity comprises no greater than about
10 mass % of one or more Group IV base stock and/or Group V base
stock.
3. A lubricating oil composition, as claimed in claim 1, wherein
said oil of lubricating viscosity consists essentially of Group III
base stock.
4. A lubricating oil composition, as claimed in claim 1, having a
sulfated ash content of from about 0.7 to about 1.0 mass %.
5. A lubricating oil composition, as claimed in claim 1, having a
phosphorus content of from about 0.08 to about 0.12 mass %.
6. A lubricating oil composition, as claimed in claim 1, comprising
from about 0.3 to about 5 mass % of said non-hydrogenated olefin
polymer.
7. A lubricating oil composition, as claimed in claim 1, comprising
from about 0.5 to about 5.0 mass % of said non-hydrogenated olefin
polymer.
8. A lubricating oil composition, as claimed in claim 1, wherein
said non-hydrogenated olefin polymer is selected from polybutene,
polylsobutene and mixtures thereof.
9. A lubricating oil composition, as claimed in claim 8, wherein
said non-hydrogenated olefin polymer has a number average molecular
weight of from about 450 to about 2300.
10. A lubricating oil composition, as claimed in claim 1,
containing from about 40 to about 600 ppm of boron.
11. A lubricating oil composition, as claimed in claim 10,
containing from about 50 to about 100 ppm of boron.
12. A lubricating oil composition, as claimed in claim 1, further
comprising one or more metal detergents including a magnesium
detergent in an amount providing said composition with at least
about 0.09 mass % of magnesium.
13. A lubricating oil composition, as claimed in claim 12, wherein
said magnesium detergent provides said composition with at least
about 0.115 mass % of magnesium.
14. A lubricating oil composition, as claimed in claim 1, having a
TBN of from 7 to about 15.
15. A lubricating oil composition, as claimed in claim 1, further
comprising a molybdenum compound in an amount providing said
composition with from about 10 to about 350 ppm of molybdenum.
16. A lubricating oil composition, as claimed in claim 1, further
comprising at least about 0.5 mass % of an ashless antioxidant
selected from the group consisting of sulfur-free phenolic
antioxidants, aminic antioxidants, and mixtures thereof.
17. A lubricating oil composition, as claimed in claim 1, further
comprising at least one nitrogen-containing dispersant, in an
amount providing said lubricating oil composition with at least
0.08 mass % of nitrogen.
18. A lubricating oil composition, as claimed in claim 17, wherein
said nitrogen-containing dispersant comprises at least one
dispersant derived from highly reactive polyisobutylene.
19. A lubricating oil composition, as claimed in claim 1, further
comprising a minor amount of at least one soot dispersing compound
of the formula: ##STR00003## where each Ar independently represents
an aromatic moiety having 0 to 3 substituents selected from alkyl,
alkoxy, alkoxyalkyl, hydroxy, hydroxyalkyl, acyloxy, acyloxyalkyl,
aryloxy, aryloxy alkyl, halo and combinations thereof; each L is
independently a linking moiety comprising a carbon-carbon single
bond or a linking group; each Y' is independently a moiety of the
formula Z(O(CR.sub.2).sub.n).sub.yX--, where X is selected from
(CR'.sub.2).sub.z, O and S; R and R' are each independently
selected from H, C.sub.1 to C.sub.6 alkyl and aryl; z is 1 to 10; n
is 0 to 10 when X is (CR'.sub.2).sub.z, and 2 to 10 when X is O or
S; y is 1 to 30; Z is H, an acyl group, an alkyl group or an aryl
group; each a is independently 0 to 3, at least one Ar moiety bears
at least one group Y in which Z is not H; and m is 1 to 100.
20. A lubricating oil composition, as claimed in claim 1, further
comprising a minor amount of a linear block copolymer comprising
one block derived primarily from vinyl aromatic hydrocarbon
monomer, and one block derived primarily from diene monomer.
21. An SAE 0W or 5W multigrade lubricating oil composition having a
sulfated ash content of no greater than 0.1 mass %, a sulfur
content of no greater than 0.4 mass %, and a phosphorus content of
from about 0.08 to 0.12 mass %; and a TBN of from about 7 to about
15 and meeting the wear performance requirements of at least one of
API CJ-4, API CI-4, and ACEA E7, said lubricating oil composition
comprising: (a) a major amount of oil of lubricating viscosity
wherein said oil of lubricating viscosity comprises no greater than
about 10 mass % of one or more Group IV base stock and/or Group V
base stock; (b) 0.3 to about 5.0 mass % of a non-hydrogenated
olefin polymer having a number average molecular weight of from
about 450 to about 2300, selected from the group consisting of
polybutene, polylsobutene and mixtures thereof; (c) an amount of an
overbased magnesium detergent providing said lubricating oil
composition with at least 0.09 mass % of magnesium; (c) at least
0.5 mass % of an ashless antioxidant selected from the group
consisting of sulfur-free phenolic antioxidants, aminic
antioxidants, and mixtures thereof; (d) at least one
nitrogen-containing dispersant, in an amount providing said
lubricating oil composition with at least 0.08 mass % of nitrogen;
and (e) a molybdenum compound in an amount providing said
lubricating oil composition with from about 10 to about 350 ppm of
molybdenum; wherein said lubricating oil composition has a boron
content of from about 50 to about 100 ppm.
22. A lubricating oil composition, as claimed in claim 21, wherein
said oil of lubricating viscosity consists essentially of Group III
base stock.
23. A lubricating oil composition, as claimed in claim 21, further
comprising a minor amount of at least one soot dispersing compound
of the formula: ##STR00004## where each Ar independently represents
an aromatic moiety having 0 to 3 substituents selected from alkyl,
alkoxy, alkoxyalkyl, hydroxy, hydroxyalkyl, acyloxy, acyloxyalkyl,
aryloxy, aryloxy alkyl, halo and combinations thereof; each L is
independently a linking moiety comprising a carbon-carbon single
bond or a linking group; each Y' is independently a moiety of the
formula Z(O(CR.sub.2).sub.n).sub.yX--, where X is selected from
(CR'.sub.2).sub.z, O and S; R and R' are each independently
selected from H, C.sub.1 to C.sub.6 alkyl and aryl; z is 1 to 10; n
is 0 to 10 when X is (CR'.sub.2).sub.z, and 2 to 10 when X is O or
S; y is 1 to 30; Z is H, an acyl group, an alkyl group or an aryl
group; each a is independently 0 to 3, at least one Ar moiety bears
at least one group Y in which Z is not H; and m is 1 to 100.
24. A lubricating oil composition, as claimed in claim 21, further
comprising a minor amount of a linear block copolymer comprising
one block derived primarily from vinyl aromatic hydrocarbon
monomer, and one block derived primarily from diene monomer.
25. A heavy duty diesel (HDD) engine lubricated with a lubricating
oil composition as claimed in claim 1.
26. A heavy duty diesel (HDD) engine lubricated with a lubricating
oil composition as claimed in claim 21.
27. A method for improving the wear performance of a heavy duty
diesel (HDD) engine, which method comprises the steps of
lubricating the engine with a lubricating oil composition, as
claimed in claim 1, and operating the lubricated engine.
28. A method for improving the wear performance of a heavy duty
diesel (HDD) engine, which method comprises the steps of
lubricating the engine with a lubricating oil composition, as
claimed in claim 21, and operating the lubricated engine.
Description
FIELD OF THE INVENTION
[0001] The present invention relates to SAE 0W and SAE 5W
multigrade crankcase lubricants for heavy duty diesel (HDD) engines
that have less than 50 mass % of Group IV and Group V base stock,
containing phosphoras-based antiwear agents in an amount
introducing no greater than 1200 ppm of phosphorus into the
lubricant, which lubricants meet the wear performance requirements
of API CJ-4, API CI-4 and/or ACEA E7 specifications.
BACKGROUND OF THE INVENTION
[0002] Crankcase lubricants comprise base stock and additives that
delay degradation of the base stock and improve its performance.
Such additives typically include dispersant, overbased and neutral
salts of organic acids, corrosion inhibitors, antiwear agents,
antioxidants, friction modifiers, antifoamants, and demulsifiers.
These additives may be combined in a package, sometimes referred to
as a detergent inhibitor (or DI) package. The additives in such a
package may include functionalized polymers, but these have
relatively short chains, typically having a number average
molecular weight M.sub.n of not more than 7000.
[0003] Multigrade lubricants perform over wide temperature ranges.
Typically, they are identified by two numbers such as 10W-30 or
5W-30. The first number in the multigrade designation is associated
with a safe cranking temperature (e.g., -20.degree. C.) viscosity
requirement for that multigrade oil as measured by a cold cranking
simulator (CCS) under high shear rates (ASTM D5293). In general,
lubricants that have low CCS viscosities allow the engine to crank
more easily at lower temperatures and thus improve engine
startability at those ambient temperatures.
[0004] The second number in the multigrade designation is
associated with a lubricant's viscosity under normal operating
temperatures and is measured in terms of the kinematic viscosity
(kV) at 100.degree. C. (ASTM D445). The high temperature viscosity
requirement brackets minimum and maximum kinematic viscosity at
100.degree. C. Viscosity at high temperatures is desirable to
prevent engine wear that would result if the lubricant thinned out
too much during engine operation. However the lubricant should not
be too viscous because excessive viscosity may cause unnecessary
viscous drag and work to pump the lubricant which in turn can
increase fuel consumption. In general, the lower a lubricants' kV
100.degree. C., the better the scores that lubricant achieves in
fuel economy tests.
[0005] Thus, in order to qualify for a given multigrade oil
designation a particular multigrade oil must simultaneously meet
both strict low and high temperature viscosity requirements that
are set by SAE specifications such as SAE J300. The current
viscosity limits set in SAE J300 are as follows:
TABLE-US-00001 SAE VISCOSITY GRADES SAE Maximum CCS
kV.sub.100.degree. C. viscosity Viscosity (mm.sup.2/s)
kV.sub.100.degree. C. (mm.sup.2/s) grade (10.sup.-3Pa s @ (.degree.
C.)) minimum maximum 0 W 3250 (-30) 3.8 5 W 3500 (-25) 3.8 -- 10 W
3500 (-20) 4.1 -- 15 W 3500 (-15) 5.6 -- 20 W 4500 (-10) 5.6 -- 25
W 6000 (-5) 9.3 -- 20 -- 5.6 <9.3 30 -- 9.3 <12.5 40 -- 12.5
<16.3 50 -- 16.3 <21.9 60 -- 21.9 <26.1
[0006] In the SAE J300 scheme multigrade oils meet the requirements
of both low temperature and high temperature performance. For
example, an SAE 5W-30 multigrade oil has viscosity characteristics
that satisfy both the 5W and the 30 viscosity grade
requirements--i.e., a maximum CCS viscosity of 3500.times.10.sup.-3
Pa.s at -25.degree. C., a minimum kV.sub.100.degree. C. of 9.3
mm.sup.2/s and a maximum kV.sub.100 .degree.of <12.5
mm.sup.2/s.
[0007] The viscosity characteristics of a lubricant depend
primarily on the viscosity characteristics of the base stock and on
the viscosity characteristics of the viscosity modifier. Of the
other additives often found in lubricants only high molecular
weight dispersants have been thought to influence viscometrics, and
their influence has been deemed small in comparison to base stock
and viscosity modifier.
[0008] The viscosity characteristic of a base stock on which a
lubricating oil is based is typically expressed by the neutral
number of the oil (e.g., S150N) with a higher neutral number being
associated with a higher viscosity at a given temperature. This
number is defined as the viscosity of the base stock at 40.degree.
C. measured in Saybolt Universal Seconds. Blending base stocks is
one way of modifying the viscosity properties of the resulting
lubricating oil. For example a lubricant formulated entirely with
S100N will have both a lower kV 100 and a lower CCS than a
lubricant formulated entirely with a S150N base stock. A base stock
comprised of a blend of S100N and S150N will have a CCS in between
those of the straight cuts. The average base stock neutral number
(ave. BSNN) of a blend of straight cuts may be determined according
to the following formula:
log ( ave . BSNN ) = [ BSR 1 .times. log BSNN 1 100 ] + [ BSR 2
.times. log BSNN 2 100 ] + [ BSRn .times. log BSNNn 100 ] where
BSRn = base stock ratio for base stock n = ( wt . % base stock n /
wt . % total base stock in oil ) .times. 100 % BSNNn = base stock
neutral number for base stock n ##EQU00001##
[0009] Merely blending base stocks of different viscosity
characteristics may not enable the formulator to meet the low and
high temperature viscosity requirements of some multigrade oils.
The formulator's primary tool for achieving this goal is an
additive conventionally referred to as a viscosity modifier or
viscosity index (V.I.) improver. Usually, to reach the minimum high
temperature viscosity required, it is necessary to add significant
amounts of viscosity modifier. However, the use of an increased
amount of viscosity modifier results in increased low temperature
lubricant viscosity. The ever increasing need to formulate
crankcase lubricants that deliver improved performance in fuel
economy tests is driving the industry to HDD engine lubricants in
the lower viscosity grades, such as 0W20, 0W30, 5W20 and 5W30.
[0010] Concurrent with the demand for lower viscosity, high fuel
economy lubricants, there has been a continued effort to reduce the
content of sulfated ash, phosphorus and sulfur in the crankcase
lubricant due to both environmental concerns and to insure
compatibility with pollution control devices used in combination
with modern engines (e.g., three-way catalytic converters and
particulate traps). A particularly effective class of
antioxidant-antiwear additives available to lubricant formulators
is metal salts of dialkyldithiophosphates, particularly zinc salts
thereof, commonly referred to as ZDDP. While such additives provide
excellent performance, ZDDP contributes each of sulfated ash,
phosphorus and sulfur to lubricants.
[0011] The most recent specifications for heavy duty diesel (HDD)
engine crankcase lubricants in each of Europe (ACEA E7) and the
United States (API CJ-4) require reductions in allowable levels of
sulfated ash, phosphorus and sulfur relative to the prior standard,
thus limiting the amount of ZDDP that can be used. At the same
time, modern lubricants are required to provide improved wear
protection. Where reduced amounts of ZDDP are employed, alternative
means of providing engine wear protection must be identified,
preferably means that do not cause introduction of additional
sulfated ash, phosphorus and/or sulfur into the lubricant.
Alternative means of providing wear protection are particularly
critical in low viscosity lubricants formulated with lower
viscosity base stocks which, as noted above, are less capable of
contributing to antiwear performance at high temperature.
[0012] To provide low viscosity, low phosphorus lubricating oil
compositions capable of meeting API CJ-4; API CI-4 and/or ACEA E7
performance standards, lubricant manufacturers have formulated
fully synthetic, lubricants and lubricants containing significant
proportions of synthetic base stocks defined as Group IV base
stocks (polyalphaolefin or PAO base stocks) and/ or Group V base
stocks, such as ester base stocks. Compared to Group I, Group II
and Group III base stocks, Group IV and Group V base stocks have a
high viscosity index (VI), which means that the kinematic viscosity
of the base stock varies less with temperature. Thus, by using a
low viscosity, high VI PAO, for example, a lubricant can be
provided having a low CCS viscosity and high kV100. However, Group
IV and Group V base stocks are expensive relative to Group I, Group
II and Group III mineral oil base stocks.
[0013] Therefore, it would be advantageous to provide a means for
blending low viscosity SAE 0W and SAE 5W multigrade crankcase
lubricants for heavy duty diesel (HDD) engines having reduced
amounts, such less than 30 mass %, of Group IV and/or Group V base
stock, and phosphorus-based antiwear agents in amounts introducing
no greater than 1200 ppm of phosphorus into the lubricant, which
lubricants meet the wear performance requirements of API CJ-4; API
CI-4; and/or ACEA E7 specifications.
[0014] Surprisingly, it has been found that SAE 0W and SAE 5W
multigrade crankcase lubricants for heavy duty diesel (HDD) engines
having less than 30 mass %, of Group IV and/or Group V base stock,
and phosphorus-based antiwear agents in amounts introducing no
greater than 1200 ppm of phosphorus into the lubricant, can meet
the performance requirements, including the wear performance
requirements of the API CJ-4; API CI-4; and/or ACEA E7
specifications when formulated with a minor amount of a
non-hydrogenated olefin polymer and at least 40 ppm of boron.
SUMMARY OF THE INVENTION
[0015] In accordance with a first aspect of the invention, there is
provided a SAE 0W and SAE 5W multigrade crankcase lubricating oil
composition for heavy duty diesel (HDD) engines meeting the
performance requirements of at least one of the API CJ-4; API CI-4;
and/or ACEA E7 specifications, having a sulfated ash content of no
greater than 1.0 mass %, such as from about 0.7 to 1.0 mass %, a
sulfur content of no greater than 0.4 mass %, and a phosphorus
content of no greater than 0.12 mass % (1200 ppm), such as from
about 0.08 to 0.12 mass %; which lubricating oil composition
comprises a major amount of oil of lubricating viscosity including
less than about 30 mass %, preferably less than 10 mass %, based on
the total mass of oil of lubricating viscosity, of Group IV and/or
Group V base stock, at least 0.3 mass %, such as 0.3 to 5 mass %,
of a non-hydrogenated olefin polymer; and greater than about 40
ppm, such as 40 to 600 ppm, of boron.
[0016] In accordance with a second aspect of the invention, there
is provided a lubricating oil composition, as described in the
first aspect, having a TBN of from about 7 to about 15.
[0017] In accordance with a third aspect of the invention, there is
provided a lubricating oil composition, as described in the first
or second aspect, comprising a magnesium detergent in an amount
providing said composition with at least 0.09 mass % (900 ppm),
preferably at least 0.10 mass % (1000 ppm), more preferably at
least 0.115 mass % (1150 ppm) of magnesium.
[0018] In accordance with a fourth aspect of the invention, there
is provided a lubricating oil composition, as described in the
first, second or third aspect, further comprising a
nitrogen-containing dispersant in an amount providing the
lubricating oil composition with at least 0.08 mass % of
nitrogen.
[0019] In accordance with a fifth aspect of the invention, there is
provided a lubricating oil composition, as described in the first
through fourth aspects, comprising at least 0.5 mass %, such as at
least 0.6 mass %, preferably at least 0.8 mass %, more preferably
at least 1.0 mass % of at least one ashless antioxidant selected
from sulfur-free hindered phenol antioxidants, aminic antioxidants,
and combinations thereof.
[0020] In accordance with a sixth aspect of the invention, there is
provided a heavy duty diesel (HDD) engine, lubricated with a
lubricating oil composition as described in any of the first
through fifth aspects.
[0021] In accordance with a seventh aspect of the invention, there
is provided a method for improving the fuel economy and wear
performance of a heavy duty diesel (HDD) engine, which method
comprises the steps of lubricating the engine with a lubricating
oil composition as described in any of the first through fifth
aspects, and operating the lubricated engine.
[0022] In accordance with a eighth aspect of the invention, there
is provided the use of a lubricating oil composition as described
in any of the first through fifth aspects to improve the fuel
economy and wear performance of a heavy duty diesel (HDD)
engine.
[0023] 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
[0024] The oil of lubricating viscosity useful in the practice of
the invention may range in viscosity from about 2 mm.sup.2/sec
(centistokes) to about 40 mm.sup.2/sec, especially from about 3
mm.sup.2/sec to about 20 mn.sup.2/sec, most preferably from about 9
mm.sup.2/sec to about 17 mm.sup.2/sec, measured, at 100.degree.
C.
[0025] Natural oils Include animal oils and vegetable oils (e.g.,
castor oil, lard oil); liquid petroleum oils and hydrorefined,
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.
[0026] Synthetic lubricating oils include hydrocarbon oils and
halo-substituted hydrocarbon oils such as polymerized and
interpolymerized olefins (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.
[0027] 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.sub.3-C.sub.8 fatty acid esters and
C.sub.13 Oxo acid diester of tetraethylene glycol.
[0028] 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-ethylhexyI
alcohol, ethylene glycol, diethylene glycol monoether, propylene
glycol). Specific examples of such esters includes dibutyl adipate,
di(2-ethylhexyl) sebacate, di-n-hexyl fumarate, dioctyl sebacate,
diisooctyl azelate, diisodecyl azelate, dioctyl phthalate, didecyl
phthalate, dieicosyl sebacate, the 2-ethylhexyt 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.
[0029] Esters useful as synthetic oils also include those made from
C.sub.5 to C.sub.12 monocarboxylic acids and polyols and polyol
esters such as neopentyl glycol, trimethylolpropane,
pentaerythritol, dipentaerythritol and tripentaerythritol.
[0030] 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.
[0031] Other examples of base oil are gas-to-liquid ("GTL") base
oils, i.e. the base oil may be oil derived from
Fischer-Tropsch-synthesized hydrocarbons made from synthesis gas
containing hydrogen and carbon monoxide using a Fischer-Tropsch
catalyst. These hydrocarbons typically require further processing
in order to be useful as base oil. For example, they may, by
methods known in the art, be hydroisomerized; hydrocracked and
hydroisomerized; dewaxed; or hydroisomerized and dewaxed.
[0032] Definitions for the base stocks and base oils in this
invention 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 base
stocks as follows: [0033] a) Group I base stocks 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. [0034] b) Group II
base stocks 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, [0035] c) Group III base stocks
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.
[0036] d) Group IV base stocks are polyalphaolefins (PAO). [0037]
e) Group V base stocks include all other base stocks not included
in Group I, II, III, or IV.
TABLE-US-00002 [0037] TABLE 1 Analytical Methods for Base Stock
Property Test Method Saturates ASTM D 2007 Viscosity Index ASTM D
2270 Sulfur ASTM D 2622; ASTM D 4294; ASTM D 4927; ASTM D 3120
[0038] Oil of lubricating viscosity useful in the practice of the
present invention may comprise a Group I, Group II, Group III, base
stocks or base oil blends of the aforementioned base stocks. The
oil of lubricating viscosity may also comprise a base oil blend of
one or more Group I, Group II, and/or Group III base stocks and
less than 30 mass %, based on the total mass of oil of lubricating
viscosity, of one or more Group IV and/or Group V base stocks.
Preferably, the oil of lubricating viscosity is mixture of one or
more Group II and/or Group III base stock and an amount of less
than 30 mass %, preferably less than 10 mass %, based on the total
mass % of oil of lubricating viscosity, of one or more Group IV or
Group V base stocks. Particularly preferred are Group III base
stocks and base stock blends, and blends of one or more Group III
base stocks and 0 to 10 mass %, based on the total mass of oil of
lubricating viscosity, of one or more Group IV base stocks. The
base stock, or base stock blend preferably has a saturate content
of at least 65%, more preferably at least 75%, such as at least
85%.
[0039] Most preferably, the base stock, or base stock blend, has a
saturate content of greater than 90%. Preferably, the oil or oil
blend will have a sulfur content of less than 1 mass %, preferably
less than 0.6 mass %, most preferably less than 0.4 mass %, such as
less than 0.3 mass %,
[0040] Preferably the volatility of the base stock or base stock
blend, as measured by the Noack test (ASTM D5800), is less than or
equal to 30 mass %, such as less than about 25 mass %, preferably
less than or equal to 20 mass %, more preferably less than or equal
to 15 mass %, most preferably less than or equal 13 mass %.
Preferably, the viscosity index (VI) of the base stock or base
stock blend is at least 85, preferably at least 100, most
preferably from about 105 to 140.
[0041] A certain amount of oil of lubricating viscosity may be
introduced into the lubricating oil composition as a diluent for
the various additives and are commonly Group I base stocks. The
preferred mass percentages, saturates contents, Noack and VI
described above are for the base stock or base stock blends used to
formulate the lubricating oil composition, excluding any oil that
may be introduced as an additive diluent.
[0042] The non-hydrogenated olefin (co)polymer useful in the
practice of the present invention is preferably a polymer or
copolymer of one or more acyclic olefin monomers. Generally, the
non-hydrogenated olefin (co)polymers useful in the invention have,
or have on average, about one double bond per polymer chain.
[0043] The (co)polymer may be prepared by polymerizing alpha-olefin
monomer, or mixtures of alpha-olefin monomers, or mixtures
comprising ethylene and at least one C.sub.3 to C.sub.28
alpha-olefin monomer, in the presence of a catalyst system
comprising at least one metallocene (e.g., a
cyclopentadienyl-transition metal compound) and an alumoxane
compound. Using this process, a polymer in which 95% or more of the
polymer chains possess terminal ethenylidene-type unsaturation can
be provided. The percentage of polymer chains exhibiting terminal
ethenylidene unsaturation may be determined by FTIR spectroscopic
analysis, titration, or C.sup.13 NMR. Interpolymers of this latter
type may be characterized by the formula
POLY-C(R.sup.1).dbd.CH.sub.2 wherein R.sup.1 is C.sub.1 to C.sub.26
alkyl, preferably C.sub.1 to C.sub.18 alkyl, more preferably
C.sub.1 to C.sub.8 alkyl, and most preferably C.sub.1 to C.sub.2
alkyl, (e.g., methyl or ethyl) and wherein POLY represents the
polymer chain. The chain length of the R.sup.1 alkyl group will
vary depending on the comonomer(s) selected for use in the
polymerization. A minor amount of the polymer chains can contain
terminal ethenyl, i.e. vinyl, unsaturation, i.e.
POLY-CH.dbd.CH.sub.2, and a portion of the polymers can contain
internal monounsaturation, e.g., POLY-CH.dbd.CH(R.sup.1), wherein
R.sup.1 is as defined above. These terminally unsaturated
interpolymers may be prepared by known metallocene chemistry and
may also be prepared as described in U.S. Pat. Nos. 5,498,809;
5,663,130; 5,705,577; 5,814,715; 6,022,929 and 6,030,930.
[0044] Another useful class of (co)polymers is (co)polymers
prepared by cationic polymerization of isobutene, styrene, and the
like. Common (co)polymers from this class include polyisobutenes
obtained by polymerization of a C.sub.4 refinery stream, having a
butene content of about 35 to about 75 mass %., and an isobutene
content of about 30 to about 60% by wt, in the presence of a Lewis
acid catalyst, such as aluminum trichloride or boron trifluoride,
with aluminium trichloride preferred. A preferred source of monomer
for making poly-n-butenes is petroleum feedstreams such as
Raffinate II. These feedstocks are disclosed in the art such as in
U.S. Pat. No. 4,952,739. Polyisobutylene is a most preferred
polymer of the present invention because it is readily available by
cationic polymerization from butene streams (e.g., using AlCl.sub.3
or BF.sub.3 catalysts). Such polyisobutylenes generally contain
residual unsaturation in amounts of about one ethylenic double bond
per polymer chain, positioned along the chain. A preferred
embodiment utilizes polyisobutylene prepared from a pure
isobutylene stream or a Raffinate I stream to prepare reactive
isobutylene polymers with terminal vinylidene olefins. Preferably,
these polymers, referred to as highly reactive polyisobutylene
(HR-PIB), have a terminal vinylidene content of at least 65%, e.g.,
70%, more preferably at least 80%, most preferably, at least 85%.
The preparation of such polymers is described, for example, in U.S.
Pat. No. 4,152,499. HR-PIB is known and is commercially available,
for example, under the tradenames Glissopal.TM. (from BASF) and
Ultravis.TM. (from BP-Amoco).
[0045] In another embodiment, the non-hydrogenated olefin
(co)polymer, for example, polyisobutylene, has at most 10, such as
5 to 10, %, of the polymer chains possessing a terminal double bond
(or terminal ethenylidene-type or terminal vinylidene
unsaturation). Such a polymer is considered not highly reactive; an
example of a commercially available polymer is under tradename
Napvis.TM. (from BP-Amoco), and usually obtained by polymerization
with aluminium trichloride as catalyst.
[0046] Preferably the (co)polymer is derived from polymerisation of
one or more olefins having 2 to 10, such as 3 to 8, carbon atoms.
An especially preferred olefin is butene, advantageously
isobutene.
[0047] The number average molecular weight of the non-hydrogenated
olefin (co)polymer useful in the present invention is preferably in
the range of from about 450 to about 2300, such as from about 450
to about 1300, preferably from about 450 to about 950. The
molecular weight can be determined by several known techniques. A
convenient method for such determination is by gel permeation
chromatography (GPC), which additionally provides molecular weight
distribution information (see W. W. Yau, J. J. Kirkland and D. D.
Bly. "Modern Size Exclusion Liquid Chromatography", John Wiley and
Sons, New York, 1979). Further, it is preferred that the kinematic
viscosity of the non-hydrogenated olefin polymer at 100.degree. C.,
as measured according to ASTM D445, is at least 9 or 15, such as
100 or 150 to 3000, advantageously 200 to 2500 or 2700
mm.sup.2s.sup.-1. In one embodiment of the present invention, a
polyisobutylene polymer having a number average molecular weight of
450 to 2300, and a kinematic viscosity at 100.degree. C. of from
about 200 to 2400 mm.sup.2s.sup.-1 was found to provide
particularly beneficial properties. Lubricating oil compositions of
the present invention can contain the non-hydrogenated olefin
polymer in an amount of at least 0.3 mass %, such as from about 0.3
to about 5.0 mass %, particularly from about 0.5 to about 3.0 mass
%, preferably from about 1.0 to about 2.5 mass %. Preferably,
lubricating oil compositions of the present invention contain less
than about 35 mass %, preferably less than about 15 mass %, based
on the combined total mass of oil of lubricating viscosity and
non-hydrogenated olefin polymer, of a combination of Group IV
and/or Group V base stock and non-hydrogenated olefin polymer.
[0048] Lubricating oil compositions of the present invention
contain greater than about 40 ppm, such as 40 to 600 ppm,
preferably from about 50 to 200 ppm, more preferably from about 50
to 100 ppm of boron. The boron can be introduced into the
lubricating oil composition by a borated dispersant, a borated
detergent, or other boron-containing additive, or a mixture
thereof, or by addition of elemental boron or other boron
compound.
[0049] Metal-containing or ash-forming detergents 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 have a total base number
or TBN (as can be measured by ASTM D2896) of from 0 to less than
150, such as 0 to about 80 or 100. 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 have a TBN of 150 or greater, and typically
will have a TBN of from 250 to 450 or more.
[0050] 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.
Combinations of detergents, whether overbased or neutral or both,
may be used.
[0051] 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.
[0052] 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 final product but typically ranges from
about 100 to 220 mass % (preferably at least 125 mass %) of that
stoichiometrically required.
[0053] 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.
[0054] 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 hetero
atoms, 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.
[0055] 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.
[0056] 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.
[0057] 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,
sulfonates/phenates/salicylates, as described, for example, in U.S.
Pat. Nos. 6,153,565; 6,281,179; 6,429,178; and 6,429,178.
[0058] Borated detergents and methods for borating detergents are
well known and described, for example, in U.S. Pat. Nos. 3,929,650;
3,480,548; and 4,792,410. Borated detergents can be used to provide
the lubricating oil compositions of the present invention with all,
or a portion, of the requisite amount of boron.
[0059] Lubricating oil compositions of the present invention
preferably contain a magnesium detergent, more preferably an
overbased magnesium detergent, in an amount providing the
lubricating oil composition with at least 0.09 mass % (900 ppm),
preferably at least 0.10 mass % (1000 ppm), more preferably at
least 0.115 mass % (1150 ppm) of elemental magnesium. Preferably,
the overbased magnesium detergent will have, or have on average, a
TBN of at least about 200, such as from about 200 to about 500;
preferably at least about 250, such as from about 250 to about 500;
more preferably at least about 300, such as from about 300 to about
450.
[0060] Overbased ash-containing detergents based on metals other
than magnesium are preferably present in amounts contributing no
greater than 40% of the TBN of the lubricating oil composition
contributed by overbased detergent. More preferably, lubricating
oil compositions of the present invention contain overbased
ash-containing detergents based on metals other than magnesium in
amounts providing no greater than about 20% of the total TBN
contributed to the lubricating oil composition by overbased
detergent.
[0061] Lubricating oil compositions of the present invention may
also contain ashless (metal-free) detergents such as oil-soluble
hydrocarbyl phenol aldehyde condensates described, for example, in
US-2005-0277559-A1.
[0062] Preferably, detergent in total is used in an amount
providing the lubricating oil composition with from about 0.35 to
about 1.0 mass %, such as from about 0.5 to about 0.9 mass %, more
preferably from about 0.6 to about 0.8 mass % of sulfated ash
(SASH). Preferably, the lubricating oil composition has a TBN of
from about 7 to about 15, such as from about 8 to about 13, more
preferably from about 9 to about 11. TBN may be contributed to the
lubricating oil composition by additives other than detergents.
Dispersants, antioxidants and antiwear agents may in some cases
contribute 40% or more of the total amount of lubricant TBN.
[0063] Conventionally, lubricating oil compositions formulated for
use in a heavy duty diesel engine comprise from about 0.5 to about
10 mass %, preferably from about 1.5 to about 5 mass %, most
preferably from about 2 to about 3 mass % of detergent, based on
the total mass of the formulated lubricating oil composition.
Detergents are conventionally formed in diluent oil.
Conventionally, detergents are referred to by the TBN, which is the
TBN of the active detergent in the diluent. Therefore, while other
additives are often referred to in terms of the amount of active
ingredient (A.I.), stated amounts of detergent refer to the total
mass of detergent including diluent.
[0064] 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 in amounts of 0.1 to 10, preferably 0.2 to 2
mass %, based upon the total weight of the lubricating oil
composition. They 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.sub.2S.sub.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.
[0065] The preferred zinc dihydrocarbyl dithiophosphates are oil
soluble salts of dihydrocarbyl dithiophosphoric acids and may be
represented by the following formula:
##STR00001##
wherein R and R' 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'
groups are alkyl groups of 2 to 8 carbon atoms. Thus, the radicals
may, for example, be ethyl, n-propyl, i-propyl, n-butyl, i-butyl,
sec-butyl, amyl, n-hexyl, i-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. R and R') in the
dithiophosphoric acid will generally be about 5 or greater. The
zinc dihydrocarbyl dithiophosphate (ZDDP) can therefore comprise
zinc dialkyl dithiophosphates. Lubricating oil compositions of the
present invention have a phosphorous content of no greater than
about 0.12 mass % (1200 ppm). Conventionally, ZDDP is used in an
amount close or equal to the maximum amount allowed. Thus,
lubricating oil compositions in accordance with the present
invention, formulated for use in heavy duty diesel engines, will
preferably contain ZDDP or other metal salt of a dihydrocarbyl
dithiophosphate, in an amount introducing from about 0.08 to about
0.12 mass % of phosphorus, based on the total mass of the
lubricating oil composition. Preferably, ZDDP is the sole
phosphorus-containing additive present.
[0066] 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.sub.5 to C.sub.12 alkyl
side chains, calcium nonylphenol sulfide, oil soluble phenates and
sulfurized phenates, phosphosulfurized or sulfurized hydrocarbons
or esters, phosphorous esters, metal thiocarbamates, oil soluble
copper compounds as described in U.S. Pat. No. 4,867,890, and
molybdenum-containing compounds.
[0067] Aromatic amines having at least two aromatic groups attached
directly to the nitrogen constitute another class of compounds that
is frequently used for antioxidancy. Typical oil soluble aromatic
amines having at least two aromatic groups attached directly to one
amine nitrogen contain from 6 to 16 carbon atoms. The amines may
contain more than two aromatic groups. Compounds having a total of
at least three aromatic groups in which two aromatic groups are
linked by a covalent bond or by an atom or group (e.g., an oxygen
or sulfur atom, or a --CO--, --S.sub.2-- or alkylene group) and two
are directly attached to one amine nitrogen also considered
aromatic amines having at least two aromatic groups attached
directly to the nitrogen. The aromatic rings are typically
substituted by one or more substituents selected from alkyl,
cycloalkyl alkoxy, aryloxy, acyl acylamino, hydroxy, and nitro
groups. The amount of any such oil soluble aromatic amines having
at least two aromatic groups attached directly to one amine
nitrogen should preferably not exceed 0.4 mass %.
[0068] The antiwear agent ZDDP provides a strong antioxidant credit
to lubricants. When less ZDDP is used in order to meet phosphorus
and SASH limits, lubricant formulators must compensate for the
resulting reduction in oxidation inhibition, preferably by use of
highly effective, ashless, sulfur-free antioxidants. Lubricating
oil compositions in accordance with the present invention therefore
preferably contain at least about 0.5 mass %, preferably at least
about 0.6 mass %, such as at least 0.8 mass %, more preferably, at
least 1.0 mass % of an ashless antioxidant selected from the group
consisting of sulfur-free phenolic antioxidant, aminic antioxidant,
or a combination thereof. Preferably, lubricating oil compositions
in accordance with the present invention contain a combination of
sulfur-free phenolic antioxidant and aminic antioxidant.
[0069] Dispersants maintain in suspension materials resulting from
oxidation during use that are insoluble in oil, thus preventing
sludge flocculation and precipitation, or deposition on metal
parts. The lubricating oil composition of the present invention
comprises at least one dispersant, and may comprise a plurality of
dispersants. The dispersant or dispersants are preferably
nitrogen-containing dispersants and preferably contribute, in
total, from about 0.08 to about 0.19 mass %, such as from about
0.09 to about 0.18 mass %, most preferably from about 0.09 to about
0.16 mass % of nitrogen to the lubricating oil composition.
[0070] Dispersants useful in the context of the present invention
include the range of nitrogen-containing, ashless (metal-free)
dispersants known to be effective to reduce formation of deposits
upon use in gasoline and diesel engines, when added to lubricating
oils and comprise an oil soluble polymeric long chain backbone
having functional groups capable of associating with particles to
be dispersed. Typically, such dispersants have amine, amine-alcohol
or amide polar moieties attached to the polymer backbone, often via
a bridging group. The ashless dispersant may be, for example,
selected from oil soluble salts, esters, amino-esters, amides,
imides and oxazolines of long chain hydrocarbon-substituted mono-
and polycarboxylic acids or anhydrides thereof; thiocarboxylate
derivatives of long chain hydrocarbons; long chain aliphatic
hydrocarbons having polyamine moieties attached directly thereto;
and Mannich condensation products formed by condensing a long chain
substituted phenol with formaldehyde and polyalkylene
polyamine.
[0071] Generally, each mono- or dicarboxylic acid-producing moiety
will react with a nucleophilic group (amine or amide) and the
number of functional groups in the polyalkenyl-substituted
carboxylic acylating agent will determine the number of
nucleophilic groups in the finished dispersant.
[0072] The polyalkenyl moiety of the dispersant of the present
invention has a number average molecular weight of from about 700
to about 3000, preferably between 950 and 3000, such as between 950
and 2800, more preferably from about 950 to 2500, and most
preferably from about 950 to about 2400. In one embodiment of the
invention, the dispersant comprises a combination of a lower
molecular weight dispersant (e.g., having a number average
molecular weight of from about 700 to 1100) and a high molecular
weight dispersant having a number average molecular weight of from
about at least about 3 500, preferably between 1800 and 3000, such
as between 2000 and 2800, more preferably from about 2100 to 2500,
and most preferably from about 2150 to about 2400. The molecular
weight of a dispersant is generally expressed in terms of the
molecular weight of the polyalkenyl moiety as the precise molecular
weight range of the dispersant depends on numerous parameters
including the type of polymer used to derive the dispersant, the
number of functional groups, and the type of nucleophilic group
employed.
[0073] The polyalkenyl moiety from which the high molecular weight
dispersants are derived preferably have a narrow molecular weight
distribution (MWD), also referred to as polydispersity, as
determined by the ratio of weight average molecular weight (Mw) to
number average molecular weight (Mn). Specifically, polymers from
which the dispersants of the present invention are derived have a
Mw/Mn of from about 1.5 to about 2.0, preferably from about 1.5 to
about 1.9, most preferably from about 1.6 to about 1.8.
[0074] Suitable hydrocarbons or polymers employed in the formation
of the dispersants of the present invention include homopolymers,
interpolymers or lower molecular weight hydrocarbons. One family of
such polymers comprise polymers of ethylene and/or at least one
C.sub.3 to C.sub.28 alpha-olefin having the formula
H.sub.2C.dbd.CHR.sup.1 wherein R.sup.1 is straight or branched
chain alkyl radical comprising 1 to 26 carbon atoms and wherein the
polymer contains carbon-to-carbon unsaturation, preferably a high
degree of terminal ethenylidene unsaturation. Preferably, such
polymers comprise interpolymers of ethylene and at least one
alpha-olefin of the above formula, wherein R.sup.1 is alkyl of from
1 to 18 carbon atoms, and more preferably is alkyl of from 1 to 8
carbon atoms, and more preferably still of from 1 to 2 carbon
atoms. Therefore, useful alpha-olefin monomers and comonomers
include, for example, propylene, butene-1, hexene-1, octene-1,
4-methylpentene-1, decene-1, dodecene-1, tridecene-1,
tetradecene-1, pentadecene-1, hexadecene-1, heptadecene-1,
octadecene-1, nonadecene-1, and mixtures thereof (e.g., mixtures of
propylene and butene-1, and the like). Exemplary of such polymers
are propylene homopolymers, butene-1 homopolymers,
ethylene-propylene copolymers, ethylene-butene-1 copolymers,
propylene-butene copolymers and the like, wherein the polymer
contains at least some terminal and/or internal unsaturation.
Preferred polymers are unsaturated copolymers of ethylene and
propylene and ethylene and butene-1. The interpolymers of this
invention may contain a minor amount, e.g. 0.5 to 5 mole % of a
C.sub.4 to C.sub.18 non-conjugated diolefin comonomer. However, it
is preferred that the polymers of this invention comprise only
alpha-olefin homopolymers, interpolymers of alpha-olefin comonomers
and interpolymers of ethylene and alpha-olefin comonomers. The
molar ethylene content of the polymers employed in this invention
is preferably in the range of 0 to 80%, and more preferably 0 to
60%. When propylene and/or butene-1 are employed as comonomer(s)
with ethylene, the ethylene content of such copolymers is most
preferably between 15 and 50%, although higher or lower ethylene
contents may be present.
[0075] These polymers may be prepared by polymerizing alpha-olefin
monomer, or mixtures of alpha-olefin monomers, or mixtures
comprising ethylene and at least one C.sub.3 to C.sub.28
alpha-olefin monomer, in the presence of a catalyst system
comprising at least one metallocene (e.g., a
cyclopentadienyl-transition metal compound) and an alumoxane
compound. Using this process, a polymer in which 95% or more of the
polymer chains possess terminal ethenylidene-type unsaturation can
be provided. The percentage of polymer chains exhibiting terminal
ethenylidene unsaturation maybe determined by FTIR spectroscopic
analysis, titration, or C.sup.13 NMR. Interpolymers of this latter
type may be characterized by the formula
POLY-C(R.sup.1).dbd.CH.sub.2 wherein R.sup.1 is C.sub.1 to C.sub.26
alkyl, preferably C.sub.1 to C.sub.18 alkyl, more preferably
C.sub.1 to C.sub.8 alkyl, and most preferably C.sub.1 to C.sub.2
alkyl, (e.g., methyl or ethyl) and wherein POLY represents the
polymer chain. The chain length of the R.sup.1 alkyl group will
vary depending on the comonomer(s) selected for use in the
polymerization. A minor amount of the polymer chains can contain
terminal ethenyl, i.e., vinyl, unsaturation, i.e.
POLY-CH.dbd.CH.sub.2, and a portion of the polymers can contain
internal monounsaturation, e.g. POLY-CH.dbd.CH(R.sup.1), wherein
R.sup.1 is as defined above. These terminally unsaturated
interpolymers may be prepared by known metallocene chemistry and
may also be prepared as described in U.S. Pat. Nos. 5,498,809;
5,663,130; 5,705,577; 5,814,715; 6,022,929 and 6,030,930.
[0076] Another useful class of polymers is polymers prepared by
cationic polymerization of isobutene, styrene, and the like. Common
polymers from this class include polyisobutenes obtained by
polymerization of a C.sub.4 refinery stream having a butene content
of about 35 to about 75 mass %, and an isobutene content of about
30 to about 60 mass %, in the presence of a Lewis acid catalyst,
such as aluminum trichloride or boron trifluoride. A preferred
source of monomer for making poly-n-butenes is petroleum
feedstreams such as Raffinate II. These feedstocks are disclosed in
the art such as in U.S. Pat. No. 4,952,739. Polyisobutylene is a
most preferred backbone of the present invention because it is
readily available by cationic polymerization from butene streams
(e.g., using AlCl.sub.3 or BF.sub.3 catalysts). Such
polyisobutylenes generally contain residual unsaturation in amounts
of about one ethylenic double bond per polymer chain, positioned
along the chain. A preferred embodiment utilizes polyisobutylene
prepared from a pure isobutylene stream or a Raffinate I stream to
prepare reactive isobutylene polymers with terminal vinylidene
olefins. Preferably, these polymers, referred to as highly reactive
polyisobutylene (HR-PIB), have a terminal vinylidene content of at
least 65%, e.g., 70%, more preferably at least 80%, most
preferably, at least 85%. The preparation of such polymers is
described, for example, in U.S. Pat. No. 4,152,499. HR-PIB is known
and HR-PIB is commercially available, for example, under the
tradenames Glissopal.TM. (from BASF) and Ultravis.TM. (from
BP-Amoco).
[0077] Polyisobutylene polymers that may be employed are generally
based on a hydrocarbon chain of from about 700 to 3000. Methods for
making polyisobutylene are known. Polyisobutylene can be
functionalized by halogenation (e.g. chlorination), the thermal
"ene" reaction, or by free radical grafting using a catalyst (e.g.
peroxide), as described below.
[0078] The hydrocarbon or polymer backbone can be functionalized,
e.g., with carboxylic acid producing moieties (preferably acid or
anhydride moieties) selectively at sites of carbon-to-carbon
unsaturation on the polymer or hydrocarbon chains, or randomly
along chains using any of the three processes mentioned above or
combinations thereof, in any sequence.
[0079] Processes for reacting polymeric hydrocarbons with
unsaturated carboxylic acids, anhydrides or esters and the
preparation of derivatives from such compounds are disclosed in
U.S. Pat. Nos. 3,087,936; 3,172,892; 3,215,707; 3,231,587;
3,272,746; 3,275,554; 3,381,022; 3,442,808; 3,565,804; 3,912,764;
4,110,349; 4,234,435; 5,777,025; 5,891,953; as well as EP 0 382 450
B1; CA-1,335,895 and GB-A-1,440,219. The polymer or hydrocarbon may
be functionalized, for example, with carboxylic acid producing
moieties (preferably acid or anhydride) by reacting the polymer or
hydrocarbon under conditions that result in the addition of
functional moieties or agents, i.e., acid, anhydride, ester
moieties, etc., onto the polymer or hydrocarbon chains primarily at
sites of carbon-to-carbon unsaturation (also referred to as
ethylenic or olefinic unsaturation) using the halogen assisted
ranctionalization (e.g. chlorination) process or the thermal "ene"
reaction.
[0080] Selective functionalization can be accomplished by
halogenating, e.g., chlorinating or brominating the unsaturated
.alpha.-olefin polymer to about 1 to 8 mass %, preferably 3 to 7
mass % chlorine, or bromine, based on the weight of polymer or
hydrocarbon, by passing the chlorine or bromine through the polymer
at a temperature of 60 to 250.degree. C., preferably 110 to
160.degree. C., e.g., 120 to 140.degree. C., for about 0.5 to 10,
preferably 1 to 7 hours. The halogenated polymer or hydrocarbon
(hereinafter backbone) is then reacted with sufficient
monounsaturated reactant capable of adding the required number of
functional moieties to the backbone, e.g., monounsaturated
carboxylic reactant, at 100 to 250.degree. C., usually about
180.degree. C. to 235.degree. C., for about 0.5 to 10, e.g., 3 to 8
hours, such that the product obtained will contain the desired
number of moles of the monounsaturated carboxylic reactant per mole
of the halogenated backbones. Alternatively, the backbone and the
monounsaturated carboxylic reactant are mixed and heated while
adding chlorine to the hot material.
[0081] While chlorination normally helps increase the reactivity of
starting olefin polymers with monounsaturated functionalizing
reactant, it is not necessary with some of the polymers or
hydrocarbons contemplated for use in the present invention,
particularly those preferred polymers or hydrocarbons which possess
a high terminal bond content and reactivity. Preferably, therefore,
the backbone and the monounsaturated functionality reactant, e.g.,
carboxylic reactant, are contacted at elevated temperature to cause
an initial thermal "ene" reaction to take place, Ene reactions are
known.
[0082] The hydrocarbon or polymer backbone can be functionalized by
random attachment of functional moieties along the polymer chains
by a variety of methods. For example, the polymer, in solution or
in solid form, may be grafted with the monounsaturated carboxylic
reactant, as described above, in the presence of a free-radical
initiator. When performed in solution, the grafting takes place at
an elevated temperature in the range of about 100 to 260.degree.
C., preferably 120 to 240.degree. C. Preferably, free-radical
initiated grafting would be accomplished in a mineral lubricating
oil solution containing, e.g., 1 to 50 mass %, preferably 5 to 30
mass % polymer based on the initial total oil solution.
[0083] The free-radical initiators that may be used are peroxides,
hydroperoxides, and azo compounds, preferably those that have a
boiling point greater than about 100.degree. C. and decompose
thermally within the grafting temperature range to provide
free-radicals. Representative of these free-radical initiators are
azobutyronitrile, 2,5-dimethylhex-3-ene-2,5-bis-tertiary-butyl
peroxide and dicumene peroxide. The initiator, when used, typically
is used in an amount of between 0.005% and 1% by weight based on
the weight of the reaction mixture solution. Typically, the
aforesaid monounsaturated carboxylic reactant material and
free-radical initiator are used in a weight ratio range of from
about 1.0:1 to 30:1, preferably 3:1 to 6:1. The grafting is
preferably carried out in an inert atmosphere, such as under
nitrogen blanketing. The resulting grafted polymer is characterized
by having carboxylic acid (or ester or anhydride) moieties randomly
attached along the polymer chains: it being understood, of course,
that some of the polymer chains remain ungrafted. The free radical
grafting described above can be used for the other polymers and
hydrocarbons of the present invention.
[0084] The preferred monounsaturated reactants that are used to
functionalize the backbone comprise mono- and dicarboxylic acid
material, i.e., acid, anhydride, or acid ester material, including
(i) monounsaturated C.sub.4 to C.sub.10 dicarboxylic acid wherein
(a) the carboxyl groups are vicinyl, (i.e., located on adjacent
carbon atoms) and (b) at least one, preferably both, of said
adjacent carbon atoms are part of said mono unsaturation; (ii)
derivatives of (i) such as anhydrides or C.sub.1 to C.sub.5 alcohol
derived mono- or diesters of (i); (iii) monounsaturated C.sub.3 to
C.sub.10 monocarboxylic acid wherein the carbon-carbon double bond
is conjugated with the carboxy group, i.e., of the structure
--C.dbd.C--CO--; and (iv) derivatives of (iii) such as C.sub.1 to
C.sub.5 alcohol derived mono- or diesters of (iii). Mixtures of
monounsaturated carboxylic materials (i)-(iv) also may be used.
Upon reaction with the backbone, the monounsaturation of the
monounsaturated carboxylic reactant becomes saturated. Thus, for
example, maleic anhydride becomes backbone-substituted succinic
anhydride, and acrylic acid becomes backbone-substituted propionic
acid. Exemplary of such monounsaturated carboxylic reactants are
fumaric acid, itaconic acid, maleic acid, maleic anhydride,
chloromaleic acid, chloromaleic anhydride, acrylic acid,
methacrylic acid, crotonic acid, cinnamic acid, and lower alkyl
(e.g., C.sub.1 to C.sub.4 alkyl) acid esters of the foregoing,
e.g., methyl raaleate, ethyl fumarate, and methyl fumarate.
[0085] To provide the required functionality, the monounsaturated
carboxylic reactant, preferably maleic anhydride, typically will be
used in an amount ranging from about equimolar amount to about 100
mass % excess, preferably 5 to 50 mass % excess, based on the moles
of polymer or hydrocarbon. Unreacted excess monounsaturated
carboxylic reactant can be removed from the final dispersant
product by, for example, stripping, usually under vacuum, if
required.
[0086] The functionalized oil-soluble polymeric hydrocarbon
backbone is then derivatized with a nitrogen-containing
nucleophilic reactant, such as an amine, amino-alcohol, amide, or
mixture thereof, to form a corresponding derivative. Amine
compounds are preferred. Useful amine compounds for derivatizing
functionalized polymers comprise at least one amine and can
comprise one or more additional amine or other reactive or polar
groups. These amines may be hydrocarbyl amines or may be
predominantly hydrocarbyl amines in which the hydrocarbyl group
includes other groups, e.g., hydroxy groups, alkoxy groups, amide
groups, nitrites, imidazoline groups, and the like. Particularly
useful amine compounds include mono- and polyamines, e.g.,
polyalkene and polyoxyalkylene polyamines of about 2 to 60, such as
2 to 40 (e.g., 3 to 20) total carbon atoms having about 1 to 12,
such as 3 to 12, preferably 3 to 9, most preferably form about 6 to
about 7 nitrogen atoms per molecule. Mixtures of amine compounds
may advantageously be used, such as those prepared by reaction of
alkylene dihalide with ammonia. Preferred amines are aliphatic
saturated amines, including, for example, 1,2-diaminoethane;
1,3-diaminopropane; 1,4-diaminobutane: 1,6-diaminohexane;
polyethylene amines such as diethylene triamine; triethylene
tetramine; tetraethylene pentamine; and polypropyleneamines such as
1,2-propylene diamine; and di-(1,2-propylene)triamine. Such
polyamine mixtures, known as PAM, are commercially available.
Particularly preferred polyamine mixtures are mixtures derived by
distilling the light ends from PAM products. The resulting
mixtures, known as "heavy" PAM, or HP AM, are also commercially
available. The properties and attributes of both PAM and/or HPAM
are described, for example, in U.S. Pat. Nos. 4,938,881; 4,927,551;
5,230,714; 5,241,003; 5,565,128; 5,756,431; 5,792,730; and
5,854,186.
[0087] Other useful amine compounds include: alicyclic diamines
such as 1,4-di(aminomethyl) cyclohexane and heterocyclic nitrogen
compounds such as imidazolines. Another useful class of amines is
the polyamido and related amido-amines as disclosed in U.S. Pat.
Nos. 4,857,217; 4,956,107; 4,963,275; and 5,229,022. Also usable is
tris(hydroxymethyl)amino methane (TAM) as described in U.S. Pat.
Nos. 4,102,798; 4,113,639; 4,116,876; and UK 989,409. Dendrimers,
star-like amines, and comb-structured amines may also be used.
Similarly, one may use condensed amines, as described in U.S. Pat.
No. 5,053,152. The functionalized polymer is reacted with the amine
compound using conventional techniques as described, for example,
in U.S. Pat. Nos. 4,234,435 and 5,229,022, as well as in
EP-A-208,560.
[0088] A preferred dispersant composition is one comprising at
least one polyalkenyl succinimide, which is the reaction product of
a polyalkenyl substituted succinic anhydride (e.g., PIBSA) and a
polyamine (PAM) that has a coupling ratio of from about 0.65 to
about 1.25, preferably from about 0.8 to about 1.1, most preferably
from about 0.9 to about 1. In the context of this disclosure,
"coupling ratio" may be defined as a ratio of the number of
succinyl groups in the PIBSA to the number of primary amine groups
in the polyamine reactant.
[0089] Another class of high molecular weight ashless dispersants
comprises Mannich base condensation products. Generally, these
products are prepared by condensing about one mole of a long chain
alkyl-substituted mono- or polyhydroxy benzene with about 1 to 2.5
moles of carbonyl compound(s) (e.g., formaldehyde and
paraformaldehyde) and about 0.5 to 2 moles of polyalkylene
polyamine, as disclosed, for example, in U.S. Pat. No. 3,442,808.
Such Mannich base condensation products may include a polymer
product of a metallocene catalyzed polymerization as a substituent
on the benzene group, or may be reacted with a compound containing
such a polymer substituted on a succinic anhydride in a manner
similar to that described in U.S. Pat. No. 3,442,808. Examples of
functionalized and/or derivatized olefin polymers synthesized using
metallocene catalyst systems are described in the publications
identified supra.
[0090] The dispersant(s) of the present invention are preferably
non-polymeric (e.g., are mono- or bis-succinimides).
[0091] Dispersant(s), particularly the lower molecular weight
dispersants, may optionally be borated. Such dispersants can be
borated by conventional means, as generally taught in U.S. Pat.
Nos. 3,087,936, 3,254,025 and 5,430,105. Boration of the dispersant
is readily accomplished by treating an acyl nitrogen-containing
dispersant with a boron compound such as boron oxide, boron halide
boron acids, and esters of boron acids, in an amount sufficient to
provide from about 0.1 to about 20 atomic proportions of boron for
each mole of acylated nitrogen composition. Borated dispersants can
be used to provide the lubricating oil compositions of the present
invention with all, or a portion, of the requisite amount of
boron.
[0092] Dispersants derived from highly reactive polyisobutylene
have been found to provide lubricating oil compositions with a wear
credit relative to a corresponding dispersant derived from
conventional polyisobutylene. This wear credit is of particular
importance in lubricants containing reduced levels of
ash-containing antiwear agents, such as ZDDP. Thus, in one
preferred embodiment, at least one dispersant used in the
lubricating oil compositions of the present invention is derived
from highly reactive polyisobutylene.
[0093] Non-dispersant/detergent boron sources are prepared by
reacting a boron compound with an oil-soluble or oil-dispersible
additive or compound. Boron compounds include boron oxide, boron
oxide hydrate, boron trioxide, boron trifluoride, boron tribromide,
boron trichloride, boron acid such as boronic acid, boric acid,
tetraboric acid and metaboric acid, boron hydrides, boron amides
and various esters of boron acids. Suitable "non-dispersant boron
sources" may comprise any oil-soluble, boron-containing compound,
but preferably comprise one or more boron-containing additives
known to impart enhanced properties to lubricating oil
compositions. Such boron-containing additives include, for example,
borated dispersant VI improver; alkali metal, mixed alkali metal or
alkaline earth metal borate; borated overbased metal detergent;
borated epoxide; borate ester; and borate amide.
[0094] Alkali metal and alkaline earth metal borates are generally
hydrated particulate metal borates, which are known in the art.
Alkali metal borates include mixed alkali and alkaline earth metal
borates. These metal borates are available commercially.
Representative patents describing suitable alkali metal and
alkaline earth metal borates and their methods of manufacture
include U.S. Pat. Nos. 3,997,454; 3,819,521; 3,853.772; 3,907,601;
3,997,454; and 4,089,790.
[0095] The borated amines maybe prepared by reacting one or more of
the above boron compounds with one or more of fatty amines, e.g.,
an amine having from four to eighteen carbon atoms. Borated amines
may be prepared by reacting the amine with the boron compound at a
temperature of from 50 to 300, preferably from 100 to 250 .degree.
C. and at a ratio from 3:1 to 1:3 equivalents of amine to
equivalents of boron compound.
[0096] Borated fatty epoxides are generally the reaction product of
one or more of the above boron compounds with at least one epoxide.
The epoxide is generally an aliphatic epoxide having from 8 to 30,
preferably from 10 to 24, more preferably from 12 to 20, carbon
atoms. Examples of useful aliphatic epoxides include heptyl epoxide
and octyl epoxide. Mixtures of epoxides may also be used, for
instance commercial mixtures of epoxides having from 14 to 16
carbon atoms and from 14 to 18 carbon atoms. The borated fatty
epoxides are generally known and are described in U.S. Pat. No.
4,584,115.
[0097] Borate esters may be prepared by reacting one or more of the
above boron compounds with one or more alcohol of suitable
oleophilicity. Typically, the alcohol contains from 6 to 30, or
from 8 to 24, carbon atoms. Methods of making such borate esters
are known in the art.
[0098] The borate esters can be borated phospholipids. Such
compounds, and processes for making such compounds, are described
in EP-A-0 684 298. Borated overbased metal detergents are known in
the art where the borate substitutes the carbonate in the core
either in part or in full.
[0099] Additional additives may be incorporated into the
compositions of the invention to enable particular performance
requirements to be met. Examples of additives which may be included
in the lubricating oil compositions of the present invention are
metal rust inhibitors, viscosity index improvers, corrosion
inhibitors, oxidation inhibitors, friction modifiers, anti-foaming
agents, anti-wear agents and pour point depressants. Some are
discussed in further detail below.
[0100] In addition to the dispersants described above, lubricating
oil compositions, particularly lubricating oil compositions for HDD
engines, preferably include additives effective in the dispersion
of soot. U.S. Published Patent Application 2006/0189492 A1 to Bera
et al. discloses certain reaction products of acylating agents and
oligomers having the following structure:
##STR00002##
where each Ar independently represents an aromatic moiety having 0
to 3 substituents selected from alkyl, alkoxy, alkoxyalkyl,
hydroxy, hydroxyalkyl, acyloxy, acyloxyalkyl, aryloxy, aryloxy
alkyl, halo and combinations thereof; each L is independently a
linking moiety comprising a carbon-carbon single bond or a linking
group; each Y' is independently a moiety of the formula
Z(O(CR.sub.2).sub.n).sub.yX--, where X is selected from
(CR'.sub.2).sub.z, O and S; R and R' are each independently
selected from H, C.sub.1 to C.sub.6 alkyl and aryl; z is 1 to 10; n
is 0 to 10 when X is (CR'.sub.2).sub.z, and 2 to 10 when X is O or
S; y is 1 to 30; Z is H, an acyl group, an alkyl group or an aryl
group; each a is independently 0 to 3, at least one Ar moiety bears
at least one group Y in which Z is not H; and m is 1 to 100. Such
compounds are described as useful soot dispersants (see also U.S.
Pat. Nos. 6,495,496 and 6,750,183 and U.S. patent application Ser.
No. 11/672,660).
[0101] Friction modifiers and fuel economy agents that are
compatible with the other ingredients of the final oil may also be
included. Examples of such materials include glyceryl monoesters of
higher fatty acids, for example, glyceryl mono-oleate; esters of
long chain polyearboxylio 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.
[0102] Other known friction modifiers comprise oil-soluble
organo-molybdenum compounds. Such organo-molybdenum friction
modifiers also provide antioxidant and antiwear credits to a
lubricating oil composition. Examples of such oil soluble
organo-molybdenum compounds include dithiocarbamates,
dithiophosphates, dithiophosphinates, xanthates, thioxanthates,
sulfides, and the like, and mixtures thereof. Particularly
preferred are molybdenum dithiocarbamates, dialkyldithiophosphates,
alkyl xanthates and alkylthioxanthates.
[0103] Additionally, the molybdenum compound may be an acidic
molybdenum compound. These compounds will react with a basic
nitrogen compound as measured by ASTM test D-664 or D-2896
titration procedure and are typically hexavalent. Included are
molybdic acid, ammonium molybdate, sodium molybdate, potassium
molybdate, and other alkaline metal molybdates and other molybdenum
salts, e.g., hydrogen sodium molybdate, MoOCl.sub.4,
MoO.sub.2Br.sub.2, Mo.sub.2O.sub.3Cl.sub.6, molybdenum trioxide or
similar acidic molybdenum compounds.
[0104] Among the molybdenum compounds useful in the compositions of
this invention are organo-molybdenum compounds of the formula
Mo(ROCS.sub.2).sub.4 and
Mo(RSCS.sub.2).sub.4
wherein R is an organo group selected from the group consisting of
alkyl, aryl, aralkyl and alkoxyalkyl, generally of from 1 to 30
carbon atoms, and preferably 2 to 12 carbon atoms and most
preferably alkyl of 2 to 12 carbon atoms. Especially preferred are
the dialkyldithiocarbamates of molybdenum.
[0105] Another group of organo-molybdenum compounds useful in the
lubricating compositions of this invention are trinuclear
molybdenum compounds, especially those of the formula
Mo.sub.3S.sub.kL.sub.nQ.sub.z and mixtures thereof wherein the L
are independently selected ligands having organo groups with a
sufficient number of carbon atoms to render the compound soluble or
dispersible in the oil, n is from 1 to 4, k varies from 4 through
7, Q is selected from the group of neutral electron donating
compounds such as water, amines, alcohols, phosphines, and ethers,
and z ranges from 0 to 5 and includes non-stoichiometric values. At
least 21 total carbon atoms should be present among all the ligand
organo groups, such as at least 25, at least 30, or at least 35
carbon atoms.
[0106] The molybdenum compounds described above, in addition to
providing friction-reducing properties, also provide antiwear
credits and, therefore, molybdenum compounds have been used in
lubricating oil compositions formulated with reduced amounts of
ZDDP. When used in such reduced phosphorus lubricating oil
compositions, molybdenum compounds have been used in amounts
introducing from about 10 to about 1000 ppm, such as 10 to about
350 ppm, or 10 to about 100 ppm of molybdenum (measured as atoms of
molybdenum).
[0107] The viscosity index of the base stock is increased, or
improved, by incorporating therein certain polymeric materials that
function as viscosity modifiers (VM) or viscosity index improvers
(VII). Generally, polymeric materials useful as viscosity modifiers
are those having number average molecular weights (Mn) of from
about 5,000 to about 250,000, preferably from about 15,000 to about
200,000, more preferably from about 20,000 to about 150,000. These
viscosity modifiers can be grafted with grafting materials such as,
for example, maleic anhydride, and the grafted material can be
reacted with, for example, amines, amides, nitrogen-containing
heterocyclic compounds or alcohol, to form multifunctional
viscosity modifiers (dispersant-viscosity modifiers). Polymer
molecular weight, specifically Mn, can be determined by various
known techniques. One convenient method is gel permeation
chromatography (GPC), which additionally provides molecular weight
distribution information (see W. W. Yau, J. J. Kirkland and D. D,
Bly, "Modern Size Exclusion Liquid Chromatography", John Wiley and
Sons, New York, 1979). Another useful method for determining
molecular weight, particularly for lower molecular weight polymers,
is vapor pressure osmometry (see, e.g., ASTM D3592).
[0108] One class of diblock copolymers useful as viscosity
modifiers has been found to provide a wear credit relative to, for
example, olefin copolymer viscosity modifiers. This wear credit is
of particular importance in lubricants containing reduced levels of
ash-containing antiwear agents, such as ZDDP. Thus, in one
preferred embodiment, at least one viscosity modifier used in the
lubricating oil compositions of the present invention is a linear
diblock copolymer comprising one block derived primarily,
preferably predominantly, from vinyl aromatic hydrocarbon monomer,
and one block derived primarily, preferably predominantly, from
diene monomer. Useful vinyl aromatic hydrocarbon monomers Include
those containing from 8 to about 16 carbon atoms such as
aryl-substituted stymies, alkoxy-substituted styrenes, vinyl
naphthalene, alkyl-substituted vinyl naphthalenes and the like.
Dienes, or diolefins, contain two double bonds, commonly located in
conjugation in a 1,3 relationship. Olefins containing more than two
double bonds, sometimes referred to as polyenes, are also
considered within the definition of "diene" as used herein. Useful
dienes include those containing from 4 to about 12 carbon atoms,
preferably from 8 to about 16 carbon atoms, such as 1,3-butadiene,
isoprene, piperylene, methylpentadiene, phenylbutadiene,
3,4-dimethyl-l,3-hexadiene, 4,5-diethyl-1,3-octadiene, with
1,3-butadiene and isoprene being preferred.
[0109] As used herein in connection with polymer block composition,
"predominantly" means that the specified monomer or monomer type
that is the principle component in that polymer block is present in
an amount of at least 85% by weight of the block.
[0110] Polymers prepared with diolefins will contain ethylenic
unsaturation, and such polymers are preferably hydrogenated. When
the polymer is hydrogenated, the hydrogenation may be accomplished
using any of the techniques known in the prior art. For example,
the hydrogenation may be accomplished such that both ethylenic and
aromatic unsaturation is converted (saturated) using methods such
as those taught, for example, in U.S. Pat. Nos. 3,113,986 and
3,700,633 or the hydrogenation may be accomplished selectively such
that a significant portion of the ethylenic unsaturation is
converted while little or no aromatic unsaturation is converted as
taught, for example, in U.S. Pat. Nos. 3,634,595; 3,670,054;
3,700,633 and Re 27,145. Any of these methods can also be used to
hydrogenate polymers containing only ethylenic unsaturation and
which are free of aromatic unsaturation.
[0111] The block copolymers may include mixtures of linear diblock
polymers as disclosed above, having different molecular weights
and/or different vinyl aromatic contents as well as mixtures of
linear block copolymers having different molecular weights and/or
different vinyl aromatic contents. The use of two or more different
polymers may be preferred to a single polymer depending on the
rheological properties the product is intended to impart when used
to produce formulated engine oil. Examples of commercially
available styrene/hydrogenated isoprene linear diblock copolymers
include Infineum SV140.TM., Infineum SV150.TM. and Infineum
SV160.TM., available from Infineum USA L.P. and Infineum UK Ltd.;
Lubrizol.RTM. 7318, available from The Lubrizol Corporation; and
Septon 1001.TM. and Septon 1020.TM., available from Septon Company
of America (Kuraray Group). Suitable styrene/1,3-butadiene
hydrogenated block copolymers are sold under the tradename
Glissoviscal.TM. by BASF.
[0112] Pour point depressants (PPD), otherwise known as lube oil
flow improvers (LOFIs) lower the temperature. Compared to VM, LOFIs
generally have a lower number average molecular weight. Like VM,
LOFIs can be grafted with grafting materials such as, for example,
maleic anhydride, and the grafted material can be reacted with, for
example, amines, amides, nitrogen-containing heterocyclic compounds
or alcohol, to form multifunctional additives.
[0113] In the present invention it may be necessary to include an
additive which maintains the stability of the viscosity of the
blend. Thus, although polar group-containing additives achieve a
suitably low viscosity in the pre-blending stage it has been
observed that some compositions increase in viscosity when stored
for prolonged periods. Additives which are effective in controlling
this viscosity increase include the long chain hydrocarbons
functionalized by reaction with mono- or dicarboxylic acids or
anhydrides which are used in the preparation of the ashless
dispersants as hereinbefore disclosed. In another preferred
embodiment, the lubricating oil compositions of the present
invention contain an effective amount of a long chain hydrocarbons
functionalized by reaction with mono- or dicarboxylic acids or
anhydrides.
[0114] When lubricating compositions contain one or more of the
above-mentioned additives, each additive is typically blended into
the base oil in an amount that enables the additive to provide its
desired function. Representative effective amounts of such
additives, when used in crankcase lubricants, are listed below. All
the values listed, except for those referring to metal detergents,
are stated as mass percent active ingredient (A.I.).
TABLE-US-00003 ADDITIVE MASS % (Broad) MASS % (Preferred)
Dispersant 0.1-20 1-8 Metal Detergents 0.1-15 0.2-9 Corrosion
Inhibitor 0-5 0-1.5 Metal Dihydrocarbyl 0.1-6 0.1-4 Dithiophosphate
Antioxidant 0-5 0.01-2.5 Pour Point Depressant 0.01-5 0.01-1.5
Antifoaming Agent 0-5 0.001-0.15 Supplemental Antiwear 0-1.0 0-0.5
Agents Friction Modifier 0-5 0-1.5 Viscosity Modifier 0.01-10
0.25-3 Base stock Balance Balance
[0115] Preferably, the Noack volatility of the fully formulated
lubricating oil composition (oil of lubricating viscosity plus all
additives) will be no greater than 20 mass %, such as no greater
than 15 mass %, preferably no greater than 13 mass %.
[0116] It may be desirable, although not essential to prepare one
or more additive concentrates comprising additives (concentrates
sometimes being referred to as additive packages) whereby several
additives can be added simultaneously to the oil to form the
lubricating oil composition.
[0117] The final composition may employ from 5 to 25 mass %,
preferably 5 to 22 mass %, typically 10 to 20 mass % of the
concentrate, the remainder being oil of lubricating viscosity.
[0118] As used herein, the terms phosphorus content, boron content,
molybdenum content, magnesium content, calcium content, etc. refer
to the content as measured by ASTM D5185; and sulfated ash content
refers to the content as measured by ASTM D874.
[0119] This invention will be further understood by reference to
the following examples, wherein all parts are parts by mass, unless
otherwise noted and which include preferred embodiments of the
invention.
EXAMPLES
[0120] A SAE 5W40 grade lubricants containing base stock,
dispersant (combination of borated dispersant and non-borated
dispersant), detergent (a combination of calcium phenate, calcium
sulfonate and magnesium sulfonate detergents), ZDDP, soot
dispersant, a combination of ashless, sulfur-free phenolic and
aminic antioxidants (0.7 mass % total), a molybdenum
dithiocarbamate compound, viscosity modifier, pour point depressant
and 1 mass % of 950 Mn polybutene (PIB) was formulated consistent
with API CJ-4 and CI-4 specifications (1.0 mass % SASH; 0.4 mass %
sulfur and 0.12 mass % phosphorus) in a blend of 4 and 6 cSt. Group
III base stocks. The resulting oil had a boron content of 65 ppm, a
magnesium content of 1156 ppm, a molybdenum content of 44 ppm and a
TBN of 9.9; 79% of the TBN contributed by overbased detergent (52%
of the TBN of the composition), was provided by the overbased
magnesium detergents.
[0121] Valve train wear resulting from the use of the above
lubricant was measured in a Cummins ISB engine test; one of the
engine tests for the API CJ-4/CI-4 specifications for HDD
lubricants. The ISB engine test includes two stages. Stage 1 runs
for 100 hours to produce soot in the oil. Stage 2 is a 250 hour
cyclic portion, intended to produce heavy load on the engine in
short bursts. At the end of the test, the valve train parts are
measured for wear, reported as tappet weight loss, in milligrams,
and camshaft lobe wear, in microns.
[0122] The results achieved with the exemplified oil are shown in
Table 2.
TABLE-US-00004 TABLE 2 Oil Oil 1 Passing Limit Grade 5W40 Tappet
Weight Loss (mg.) 85 100 max Cam Shaft Lobe Wear, 43 55 max Snap
Gauge (.mu.m)
[0123] As shown, Oil 1, a 5W40 grade lubricant formulated with all
Group III base stock and having a phosphorus content of less than
1200 ppm, was able to meet the wear performance requirements of the
API CJ-4/CI-4 specifications.
[0124] The disclosures of all patents, articles and other materials
described herein are hereby incorporated, in their entirety, into
this specification by reference.
[0125] Compositions described as "comprising" a plurality of
defined components are to be construed as including compositions
formed by admixing the defined plurality of defined 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. Changes may be made by those
skilled in the art without departing from the spirit of the
invention.
* * * * *