BACKGROUND OF THE INVENTION
[0001] This invention relates to a diurea grease composition. More particularly, it relates
to a diurea grease composition which undergoes little changes in consistency after
use at higher temperatures for a prolonged period of time and small oil separtion
at higher temperatures and which is also superior in various other properties.
[0002] Up to now, metal soaps are predominantly employed as the grease thickeners. However,
the lithium soap grease, known as the "universal grease", has a dropping point of
the order of 200°C or thereabouts and cannot be used at higher temperatures above
150°C.
[0003] On the other hand, various copmlex soaps, sodium terephthalamate, bentone or organic
thickeners, such as indanthrene or urea have been proposed as high temperature long
life grease thickeners. However, these thickeners suffer from certain demerits. For
example, a calcium complex type thickener tends to be hardened markedly with lapse
of time. Sodium terephthalamate in general undergoes syneresis and oil separation
considerably, while it tends to be deteriorated due to oxidation by reason of intramolecular
metal atoms in the thickener. Bentone is inferior in lubricating properties at higher
temperatures on prolonged usage, while indanthrene has a bad hue and is expensive.
[0004] On the other hand, urea greases, such as diurea grease or tetraurea greases having
modified terminal groups, have many advantageous points as compared with the above
mentioned greases. However, the tetraurea grease tends to be hardened or increased
in consistency when exposed to higher temperatures for prolonged time period, while
it may be disadvantageously hardened or softened depending on different shearing speeds
given to the grease. The known diurea greases having only terminal alkyl groups have
a low dropping point and undergoes considerable oil separation at higher temperatures
so that they cannot be used for prolonged time at higher temperatures. The diurea
greases having only aromatic hydrocarbon terminal groups are at most equivalent or
even inferior to the diurea greases having the terminal alkyl groups with respect
to the properties as the thickener.
[0005] The present inventors have conducted researches towards overcoming the above mentioned
drawbacks of the urea greases and have found that, while the diurea compound has highly
desirable properties as the thickener, the terminal groups of the diurea compound
plays an extremely important role.
[0006] Specifically, it has been found that the diurea compound in which C-6 to C-12 cyclohexyl
groups or its derivatives and C-8 to C-20 alkyl groups exist on either one of the
terminal ends of the diurea compounds and in which the contents of the cyclohexyl
groups or its derivatives are 20 to 90 mol percent based on the total amount of the
two groups, exhibits extremely desirable properties as the grease thickener. This
diurea compound has been applied for patent in our Japanese Patent Publication No.
11156/1980.
[0007] Ths diurea grease disclosed in the Japanese Patent Publication No. 11156/1980 has
many excellent properties, such as
i) little changes in consistency after prolonged use at higher temperatures;
ii) superior mechanical stability under a wide range of shearing speeds;
iii) small oil separation at higher temperatures;
iv) superior water resistance; and
v) improved thickening properties.
[0008] A diurea grease composition exhibiting extremely low hardening properties with lapse
of time besides the above mentioned desirable properties has also been found and applied
for patent in Japanese Patent Laid-open Aplication No. 250097/1987.
[0009] Also an urea grease containing two diurea compounds at predetermined ratios which
are sandwitched between the terminal group and both urea groups and different with
respect to the hydrocarbon groups, is disclosed in our Japanese Patent Application
No. 139696/1989.
[0010] As a result of our further researches, the present inventors have found that a grease
containing a diurea compound obtained by reacting an amine with a mixed system of
two or more different diisocyanates exhibits superior properties. This finding has
led to fulfilment of the present invention.
SUMMARY OF THE INVENTION
[0011] It is a principal object of the present invention to provide a diurea grease composition
which undergoes little changes in consistency after use at higher temperatures for
prolonged time and small oil separation at higher temperatures, and which is also
superior in other various properties.
[0012] The above and other objects of the present invention will become apparent from the
following description.
[0013] In acordance with the present invention ,there is provided a diurea grease composition
comprising a base oil and 2 to 25 wt.%, based on the total weight of the composition,
of a diurea compound as an essential ingredient, the diurea grease compound being
produced by reacting a mixed system of two or more different diisocyanates represented
by the formula (I)
OCN-R-NCO (I)
wherein R stands for a straight-chained or branched alkylene group, a straight-chained
or branched alkenylene group, a cycloalkylene group or an aromatic group, with an
amine compound selected from the group consisting of a primary amine represented by
the formula (II)
R₁-NH₂ (II)
wherein R₁ stands for a hydrocarbon residue having 6 to 20 carbon atoms, a secondary
amine represented by the formula (III)

wherein R₂ and R₃ may be the same or different and each stand for hydrocarbon residues
having 6 to 20 carbon atoms, and mixtures thereof.
PREFERRED EMBODIMENTS OF THE INVENTION
[0014] The present invention will be explained in more detail hereinbelow.
[0015] As the base oils, any oils commonly used as the lube base oil may be employed. As
mineral lube base oils, mineral oils refined by a method consisting in a suitable
combination of distillation under reduced pressure, solvent deasphalting, solvent
extraction, hydrocracking, solvent dewaxing, hydrogenative dewaxing, washing by sulfuric
acid, refining by terra abla or hydrofining.
[0016] As synthetic lube oils, α-olefin oligomers, such as normal paraffins, isoparaffins,
polybutene, polyisobutyrene or 1-decene oligomers, alkylbenzenes such as monoalkylbenzene,
dialkylbenzene or polyalkylbenzene, alkyl naphthalenes, such as monoalkyl naphthalene,
dialkyl naphthalene or polyalkyl naphthalene, diesters such as di-2-ethylhexyl sebacate,
dioctyl adipate, diisodecyl adipate, ditridecyl adipate or ditridecyl glutarate, polyol
esters such as trimethylolpropane caprylate, trimethylolpropane pelargonate, pentaerithritol-2-ethyl
hexanoate or pentaerithritol pelargonate, polyglycols such as polyethylene glycol,
polyethylene glycol monoether, polypropylene glycol or polypropylene glycol monoether,
polyphenyl ethers, tricresyl phosphate, silicone oils or perfluoroalkyl ethers, may
be employed. Two or more of the above mentioned oils may also be employed as a mixture.
The desirable viscosity range of these base oils is 2 to 2000 cSt at 100°C.
[0017] The diurea compound as the essential ingredient of the composition of the present
invention may be obtained by reacting a mixed system of two or more different diisocyanates
represented by the formula (I)
OCN-R-NCO (I)
wherein R stands for a straight-chained or branched alkylene group, a straight-chained
or branched alkenylene group, a cycloalkylene group or an aromatic group, with an
amine compound selected from the group consisting of a primary amine represented by
the formula (II)
R₁-NH₂ (II)
wherein R₁ stands for a hydrocarbon residue having 6 to 20 carbon atoms, a secondary
amine represented by the formula (II)

wherein R₂ and R₃ may be the same or different and each stand for hydrocarbon residues
having 6 to 20 carbon atoms, and mixtures thereof.
[0018] The number of carbon atoms in the group R in the isocyanate represented by the formula
(I) may preferably be 6 to 20 and more preferably 6 to 15. The aforementioned mixed
system of the diisocyanates preferably include mixtures of two or more compounds selected
from the group consisting of, for example, diphenylmethane-4, 4′-diisocyanate, tolylene
diisocyanate, hexamethylene diisocyanate, 2, 2, 4-trimethyl-hexamethylene diisocyanate,
p-phenylene diisocyanate, 4, 4′-dicyclohexylmethane diisocyanate, 3, 3′-dimethyldiphenyl-4,
4′-diisocyanate, m-xylene diisocyanate, m-tetramethylxylene diisocyanate, p-tetramethylxylene
diisocyanate, isophorone diisocyanate, 1, 5-naphthalene diisocyanate and trans-1,
4-cyclohexyl diisocyanate. More specifically, it may include a mixed system of diphenylmethane-4,
4′-diisocyanate and 4, 4′-dicyclohexylmethane diisocyanate, a mixed system of diphenylmethane-4,
4′-diisocyanate and 3, 3′-dimethyldiphenyl-4, 4′-diisocyanate, a mixed system of
diphenylmethane-4, 4′-diisocyanate and m-xylenediisocyanate, a mixed system of diphenylmethane-4,
4′-diisocyanate and tetramethylxylene diisocyanate, a mixed system of diphenylmethane-4,
4′-diisocyanate and a mixture of 2, 4-tolylene diisocyanate and 2, 6-tolylene diisocyanate,
a mixed system of diphenylmethane-4, 4′-diisocyanate and isophorone diisocyanate,
a mixed system of 3, 3′-dimethyldiphenyl-4,4′-diisocyanate and m-xylene diisocyanate,
a mixed system of 3, 3′-dimethyldiphenyl-4, 4′-diisocyanate and tetramethylxylene
diisocyanate, a mixed system of 3, 3′-dimethyldiphenyl-4, 4′-diisocyanate and a mixture
of 2, 4-tolylene diisocyanate and 2, 6-tolylene diisocyanate, a mixed system of 3,
3′-dimethyldiphenyl-4, 4′-diisocyanate and hexamethylene diisocyanate, a mixed system
of m-xylene diisocynate and tetramethylxylene diisocyanate, a mixed system of m-xylene
diisocyanate and a mixture of 2, 4-tolylene diisocyanate and 2,6-tolylene diisocyanate,
a mixed system of m-xylene diisocyanate and hexamethylene diisocyanate, a mixed system
of tetramethylxylene diisocyanate and a mixture of 2, 4-tolylene diisocyanate and
2, 6-tolylene diisocyanate, a mixed system of tetramethylxylene diisocyanate and isophorone
diisocyanate, and a mixed system of a mixture of 2, 4-tolylene diisocyanate and 2,
6-tolylene diisocyanate and hexamethylene diisocyanate.
[0019] The mixing ratios of the above mentioned two or more different diisocyanates may
be suitably selected in dependence upon the structures of the diisocyanates and the
consistency of the greases to be produced. However, when mixing two different diisocyanates,
the mixing ratio may usually be 5 - 95 : 95 - 5, preferably 10 - 90 : 90 - 10, more
preferably 20 - 80 : 80 - 20 and most preferably 30 - 70 : 70 - 30, in terms of the
mol percent ratio. The mixing ratio less than the range of 5 - 95 : 95 - 5 is not
desirable since problems are raised in changes in consistency after use or in oil
separation so that the properties of the grese thickener are lowered. More specifically,
with the mixed system of diphenylmethane-4, 4′-diisocyanate represented by the formula

and tolylene diisocyanate represented by the formula

the mixing ratio is preferably 10 to 95 mol percent, prferably 20 to 80 mol percent
and most preferably 30 to 70 mol percent of diphenylmethane-4, 4′-diisocyanate and
5 to 90 mol percent, preferably 20 to 80 mol percent and most preferably 30 to 70
mol percent of tolylene diisocyanate. When using three or more diisocyanates, the
respective diisocyanates are preferably contained in amounts of not less than 5 mol
percent and preferably not less than 10 mol percent.
[0020] According to the present invention, the amine compound reacted with the mixed diisocyanate
system is a primary amine, a mixture of two or more primary amines, a secondary amine,
or a mixture of two or more different secondary amines, represented by the above formulas
(II) and (III), or mixtures thereof. In the above formulas (II) and (III), R₁, R₂
and R₃ may be the same or different groups and denote hydrocarbon residues with 6
to 20 caron atoms. As these hydrocarbon residues, various groups such as alkyl, alkenyl,
cycloalkyl or aromatic groups, may be employed. The alkyl groups may include those
with straight or branched chains, such as hexyl, heptyl, octyl, nonyl, decyl, undecyl,
dodecyl, tridecyl, tetradecyl, pentadecyl, hexadecyl, heptadecyl, octadecyl, nonadecyl
or eicosyl groups.
[0021] The alkenyl groups may include those with straight or branched chains, such as hexenyl,
heptenyl, octenyl, nonenyl, decenyl, undecenyl, dodecenyl, tridecenyl, tetradecenyl,
pentadecenyl, hexadecenyl, heptadecenyl, octadecenyl, nonadecenyl or eicosenyl groups.
[0022] As the cycloalkyl groups, cyclohexyl group and the groups derived from the cyclohexyl
group may preferably be employed. Examples of the cyclohexyl group and its derivatives
may include cyclohexyl, methyl cyclohexyl, dimethyl cyclohexyl, ethyl cyclohexyl,
diethyl cyclohexyl, propyl cyclohexyl, isopropyl cyclohexyl, 1-methyl-3-propyl-cyclohexyl,
butyl cyclohexyl, amyl cyclohexyl, amylmethyl cyclohexyl, hexyl cyclohexyl, heptyl
cyclohexyl, octyl cyclohexyl, nonyl cyclohexyl, decyl cyclohexyl, undecyl cyclohexyl,
dodecyl cyclohexyl, tridecyl cyclohexyl and tetradecyl cyclohexyl groups. Most desirable
are a cyclohexyl group and C7 to C8 groups derived from the cyclohexyl group, such
as, for example, methyl cyclohexyl, dimethyl cyclohexyl or ethyl cyclohexyl groups.
[0023] Examples of the aromatic groups may include phenyl, toluyl, benzyl, ethyl phenyl,
methyl benzyl, xylyl, propyl phenyl, cumenyl, ethyl benzyl, methyl phenetyl, butyl
phenyl, propyl benzyl, ethyl phenetyl, pentyl phenetyl, butyl benzyl, propyl phenetyl,
hexyl phenyl, pentyl benzyl, butyl phenetyl, heptyl phenyl, hexyl benzyl, pentyl phenetyl,
octyl phenyl, heptyl benzyl, hexyl phenetyl, nonyl phenyl, octyl benzyl, heptyl phenetyl,
decyl phenyl, nonyl benzyl, octyl phenetyl, undecyl phenyl, decyl benzyl, nonyl phenetyl,
dodecyl phenyl, undecyl benzyl, decyl phenetyl, tridecyl phenyl, dodecyl benzyl, undecyl
phenetyl, tetradecyl phenyl, tridecyl benzyl, dodecyl phenetyl, naphtyl, methyl naphtyl,
ethyl naphtyl, propyl naphtyl, butyl naphtyl, pentyl naphtyl, hexyl naphtyl, heptyl
naphtyl, octyl naphtyl, nonyl naphtyl and decyl naphtyl groups.
[0024] The most preferred amine compound to be reacted with the above mentioned diisocyanate
mixed system is a primary amine represented by the formula (II) in which R₁ denotes
a cyclohexyl group, a C7 to C12 alkylcyclohexyl group, a C 6 to C20 alkyl group or
a C6 to C20 alkenyl group, or a secondary amine represented by the formula (III) in
which R₂ and R₃ each denote a cyclohexyl group or a C7 to C12 alkylcyclohexyl group.
Most preferred is also an amine mixture in which the primary amine represented by
the formula (II) is used and in which the ratio of the total number of cyclohexyl
groups and/or the alkyl cyclohexyl groups to the number of the total amines given
by the formula {(total number of the cyclohexyl groups and/or the alkylcyclohexyl
groups)/(the total number of the groups selected from the group consisting of the
cyclohexyl group, alkylcyclohexyl group, alkyl group and the alkenyl group bonded
to the amine employed)} X 100 is 20 to 90 in terms of the mol percent. In this case,
contents of the diurea compound containing both the cyclohexyl groups and/or alkylcyclohexyl
groups and the alkyl groups and/or alkenyl groups in the produced diurea compound
account for 10 mol percent or higher based on the total number of the produced diurea
compounds. Also preferred is an amine mixture consisting of a primary amine of the
formula (II) in which R₁ is a cyclohexyl group, a C7 to C12 alkyl cyclohexyl group
or a C6 to C20 alkyl group and a secondary amine of the formula (III) in which R₂
and R₃ each represent a cyclohexyl group or a C7 to C12 alkyl cyclohexyl group and
in which the ratio of the contents of the secondary amine to the amount of total amine
given by the formula {(number of amino groups in the secondary amine)/(number of the
amino groups in the primary amine plus number of the amino groups in the secondary
amine)} X 100 is 1 to 50 in terms of mol percent, or an amine mixture in which the
total amount of the primary amine of the formula (II) in which R₁ is a cyclohexyl
group or an alkylcyclohexyl group bears a molar ratio of 1/4 to 4/1 with respect to
the primary amine of the formula (II) in which R₁ is an alkyl group. By using these
preferred amine mixtures, the hardening properties of the diurea grease composition
with lapse of time according to the present invention may be diminished significantly.
[0025] With the diurea grease composition of the present invention, the diurea compound,
acting as the thickener, is produced by reacting the above mentioned mixed system
of the diisocyanates with the above mentioned primary amine and/or secondary amine.
This point is most crucial in the present invention. The effects of the present invention
cannot be derived from the diurea grease obtained in any other methods, such as by
separately reacting the above mentioned two or more diisocyanates with amines and
subsequently mixing the produced two or more diurea compounds.
[0026] When the above mentioned mixed system of diisocyanates is reacted with the above
mentioned primary amine and/or the secondary amine, volatile solvents, such as benzene,
toluene, xylene, hexane, naphtha, diisobutyl ether, carbon tetrachloride or petroleum
ether, may be employed. Lube base oils may also be employed as suitable solvents.
The preferred reaction temperature is 100 to 200°C. The reaction system need be mixed
and agitated thoroughly to produce a uniform diurea grease.
[0027] The thus produced diurea compound, acting as the thickener, contains the diurea compounds
in amounts corresponding to the mixing ratios of the diisocyanates. More specifically,
if the mixed system consisting of 10 to 95 mol percent of diphenylmethane-4, 4′-diisocyanate
and 5 to 95 mol percent of tolylene diisocyanate is employed, the thickener contains
10 to 95 mol percent of a diure compound represented by the formula

and 5 to 90 mol percent of a diurea compound represented by the formula

wherein X₁, X₂, X₃ and X₄ each stand for one of the groups R₁-NH- or

where R₁, R₂ and R₃ have the same meaning as R₁, R₂ and R₃ in the above formulas
(II) and (III). When the volatile solvent is used, the solvent is removed and a suitable
amount of the lube base oil is added to give the grease. When the lube base oil is
used as the solvent, the reaction product may be used directly as the grease.
[0028] With the diurea grease composition of the present invention, the contents of the
diurea compound acting as the thickener is 2 to 25 wt.% and preferably 3 to 20 wt.%
based on the total weight of the composition. The contents of the diurea compound
less than 2 wt.% are not desirable because the effects as the thickener are nill,
whereas the contents in excess of 25 wt.% are also not desirable because the grease
becomes too hard and cannot exhibit the lubricating effects sufficiently.
[0029] The grease of the present invention may be admixed with suitable additives for further
improving its properties. These aditives amy include other thickeners, such as metal
soaps, bentone or silica gel, extreme pressure agents, such as chlorine, sulphur or
phosphorus extreme pressure agents or zinc dithiophosphate, oiliness agents such as
fatty oils, animal or vegetable oils, viscosity index improvers, such as polymethacrylate,
polybutene or polystyrene, anti-oxidants such as amine, phenol or sulpher anti-oxidants
or zinc dithiophosphate, or metal inactivators, such as benzotriazole or thiadiazole.
EXAMPLES OF THE INVENTION
[0030] The present invention will be explained in more detail with reference to certain
Examples and Comparative Examples.
Example 1
[0031] 30.5 g of diphenylmethane-4, 4′-diisocyanate and 21.2 g of tolylene diisocyanate
were charged into 895 g of mineral oil having a viscosity at 100°C of 10.3 cST and
heated to 60°C so as to be dissolved uniformly therein. 48.3 g of cyclohexylamine
were added and agitated vigorously. In this manner, a gel-like substance was produced
immediately. This substance was maintained under sustained agitation at 100°C for
30 minutes. 5 g of an anti-oxidant was added and the resulting mixture was agitated
thoroughly. The mixture was then passed through a roll mill to produce a grease composition.
The produced diurea compound was formed by 50 mol percent of the diurea compound represented
by the formula

and 50 mol percent of the diurea compound represented by the formula

The contents in the composition of the thickener formed by the diurea compound were
10 wt.%.
[0032] The following performace evaluating tests were conducted on the produced grease.
The results are shown in Table 1.
(Tests for Evaluation of the Performance)
[0034] As the consistency, the unworked consistency (UW) and the worked consistency (60W
and 10⁵W) were masured in accordance with the consistency testing method according
to ASTM 217.
[0035] The dropping point was measured in accordance with the dropping point testing method
in JIS K 2220 5.4.
[0036] The oil separation was measured at 150°C for 200 hours in accordance with the oil
separation testing method in JIS K 2220 5.7.
Example 2
[0037] 32.7 g of diphenylmethane-4, 4′-diisocyanate and 5.7 g of tolylene diisocyanate were
charged into 600 g of mineral oil having a viscosity at 100°C at 10.3 cSt and heated
to 60°C so as to be dissolved uniformly therein. To this solution was added a solution
obtained by mixing and dissolving 44.1 g of octadecylamine and 17.5 g of p-toluidine
in 300 g of dioctyl sebacate and the resulting mixture was agitated vigorously. In
this manner, a gell-like substance was produced immediately. After the agitation was
continued further so that the temperature of the gell-like substance was raised to
80°C, the substance was passed through a roll mill to produce a grease composition.
The produced diurea compound was formed by 80 mol percent in total of diurea compounds
represented by the formulas

and 20 mol percent in total of diurea compounds represented by the formulas

The contents in the composition of the thickener formed by the diurea compounds were
10 wt.%.
[0038] The performnce evaluating tests similar to those in example 1 were conducted on the
produced diurea grease. The results are shown in Table 1.
Example 3
[0039] 13.4 g of diphenylmethane-4, 4′-diisocyanate and 21.7 g of tolylene diisocyanate
were charged into 900 g of low molecular polybutene having a viscosity at 100°C of
23.5 cSt and were heated to 60°C so as to be dissolved uniformly therein. To this
solution were added 48.4 g of dicyclohexylamine and 16.5 g of laurylamine and agitated
vigorously. A gel-like substance was produced immediately. After the agitation was
continued for 30 minutes to raise the temperature to 120°C, the substance was passed
through a roll mill to produce a grease composition. The produced diurea compound
was formed by 30 mol percent in total of the diurea compounds reprsented by the formulas

and 70 mol percent in total of the diurea compounds represented by the formulas

The contents in the composition of the thickener formed by the diurea compounds were
10 wt.%.
[0040] The performance tests similar to those in Example 1 were conducted on the produced
diurea grease for evaluating the performance. The results are shown in Table 1.
Example 4
[0041] 25.3 g of diphenylmethane-4, 4′-diisocyanate and 17.6 g of tolylene diisocyanate
were charged into 600 g of a mineral oil having a viscosity at 100°C of 31.5 cSt and
were heated to 60°C so as to be dissolved uniformly therein. To this solution was
added a solution obtained by mixing and dissolving 20.0 g of cyclohexylamine and 37.1
g of laurylamine in 300 g of mineral oil and the resulting mixture was agitated vigorously.
A gel-like sustance was produced immediately. After the agitation was continued to
raise the temperature to 80°C, the substance was passed through a roll mill to produce
a grease composition. The produced diurea compound was comprised of 50 mol percent
in total of the diurea compounds represented by the formulas

50 mol percent in total of the diurea compounds represented by the formulas

with the sum of the amounts of the compounds represented by the formulas (2) and
(5) being 50 mol percent. The contents in the composition of the thickener formed
by the diurea compounds were 10 wt.%.
[0042] The performance evaluating tests similar to those in Example 1 were conducted on
the produced diurea grease. The results are shown in Table 1.
Example 5
[0043] 15.3 g of diphenylmethane-4, 4′-diisocyanate and 24.9 g of tolylene diisocyanate
were charged into 600 g of a synthetic hydrocarbon oil having a viscosity at 100°C
of 8.2 cSt and heated to 60°C so as to be dissolved uniformly therein. To this solution
was added a solution obtained by mixing and dissolving 32.9 g of octadecylamine, 12.1
g of cyclohexylamine and 14.8 g of dicyclohexylamine in 300 g of synthetic hydrocarbon
oil and the resulting mixture was agitated vigorously. A gel-like sustance was produced
immediately. After the agitation was continued to raise the temperature to 80°C, the
substance was passed through a roll mill to produce a grease composition. The produced
diurea compound was formed by 30 mol percent of a diurea compound represented by the
formula

and 70 mol percent of a diurea compound represented by the formula

at a rate of 30 : 30 :40. The contents in the composition of the thickener formed
by the diurea compounds were 10 wt.%. The performance appraisal tests similar to those
of Example 1 were conducted on the produced diurea grease. The resulta are shown in
Table 1.
Example 6
[0044] 22.9 g of diphenylmethane-4, 4′-diisocyanate and 24.0 g of tolylene diisocyanate
were charged into 600 g of polyphenyl ether having a viscosity at 100°C of 13.0 cSt
and were heated to 60°C so as to be dissolved uniformly therein. To this solution
was added a solution of 35.3g of methylcyclohexylamine and 17.8 g of octylamine in
295 g of polyphenyl ether and agitated vigorously. A gel-like substance was produced
immediately. This substance was maintained at 100°C for 30 minutes under sustained
agitation and admixed with 5 g of an anti-oxidant. The resulting mixture was agitated
thoroughly and passed through a roll mill to produce a grease composition. This diurea
compounds were formed by 40 mol percent in total of diurea compounds represented by
the formulas

and 60 mol percent in total of diurea compounds represented by the formulas

wherein the sum of the amounts of the compounds represented by the formulas (8) and
(11) is 30 mol percent and the ratio of the contents of the methylcyclohexyl group
and the octyl group is 70 : 30. The contents in the composition of the thickener formed
by the diurea compounds were 10 wt.%.
[0045] The performance appraisal tests similar to those of Example 1 were conducted on the
produced diurea grease. The results are shown in Table 1.
Example 7
[0046] 23.4 g of diphenylmethane-4, 4′-diisocyanate and 10.8 g of tolylene diisocyanate
were charged into 600 g of polyglycol having a viscosity at 100°C of 11.3 cSt and
were heated to 60°C so as to be dissolved uniformly therein. To this solution was
added a solution of 37.0 g of eicosylamine, 11.9 g of dimethylcyclohexylamine and
16.9 g of dicyclohexylamine in 300 g of polyglycol and agitated vigorously. A gel-like
substance was produced immediately. This substance was raised to a temperature of
80°C by sustained agitation and passed through a roll mill to produce a grease composition.
The produced diurea composition was formed by 60 mol percent of a diurea compound
represented by the formula

and 40 mol percent of a diurea compound represented by the formula

wherein Y₁, Y₂, Y₃ and Y₄ each represent groups

at the ratio of 40 : 30 : 30. The contents in the composition of the thickener formed
by the diurea compounds were 10 wt.%.
[0047] The performance appraisal tests similar to those of Example 1 were conducted on the
produced diurea grease. The results are shown in Table 1.
Examples 8 to 11
[0048] Diisocyanates A and B each shown in the following Table were charged into 900 g of
a mineral oil having a viscosity at 100°C of 10.3 cSt and were heated to 60°C so as
to be uniformly dissolved therein. To this solution was added cyclohexylamine in amounts
respectively shown in the Table and agitated vigorously. Each of gel-like substances
was produced immediately. After the temperature was raised to 120°C by sustaind agitation
for 30 minutes, each substance was passed through a roll mill to produce a grease
composition. The contents in the composition of the thickener formed by the diurea
compounds were 10 wt.%, respectively.
[0049] The performance apraisal tests similar to those of Example 1 were conducted on the
produced diurea greases. The results are shown in Table 1.
Table
Example |
8 |
9 |
10 |
11 |
Diisocyanate A (g) |
MDI 30.0 |
TODI 29.2 |
MDI 7.3 |
TODI 31.9 |
Diisocyanate B (g) |
XDI 22.5 |
TMXDI 27.0 |
IPDI 3.1 |
HDI 20.3 |
Cyclohexyl amine (g) |
47.5 |
43.8 |
9.6 |
47.8 |
Notes: The molar ratio of diisocyanate A to diisocyanate B is 50 : 50. |
[0050] The abbreviations used in the above Table denote the following:
MDI : 4, 4′-diphenylmethane diisocyanate
XDI : m-xylene diisocyanate
TODI : 3, 3′-dimethyldiphenyl-4, 4′-diisocyanate
TMXDI : tetramethylxylene diisocyanate
IPDI : iophorone diisocyanate
HDI : 1, 6-hexamethylene diisocyanate
Comparative Examples 1 and 2
[0051] For comparison, the performance appraisal tests similar to those of Example 1 were
conducted on the commercially available urea greases. The results are shown in Table
1.
Comparative Example 3
[0053] 55.8 g of diphenylmethane-4, 4′-diisocyanate were charged into 895 g of mineral oil
having a viscosity at 100°C of 10.3 cSt, and were heated to 60°C so as to be uniformly
dissolved therein. 44.2 g of cyclohexylamine were added to the solution and agitated
vigorously. A gel-like substance was formed immediately. This substance was maintained
at 100°C for 30 minutes under continued agitation and admixed with 5.0 g of an anti-oxidant.
The resulting mixture was agitated thoroughly and passed through a roll mill to produce
a grease.
[0054] The contents of the diurea compound of the formula

acting as the thickener were 10 wt.%.
[0055] The performance tests similar to those of Example 1 were conducted on the produced
diurea grease. The results are shown in Table 1.
Comparative Example 4
[0056] 46.8 g of tolylene diisocyanate were charged into 895 g of mineral oil having a viscosity
at 100°C of 10.3 cSt and dissolved therein. 53.2 g of cyclohexylamine were added to
the solution and agitated vigorously. A gel-like substance was formed immediately.
This substance was maintained at 100°C for 30 minutes under continued agitation and
admixed with 5.0 g of an anti-oxidant. The resulting mixture was agitated thoroughly
and passed through a roll mill to produce a grease.
[0057] The contents of the diurea compound of the formula

acting as the thickener were 10 wt.%.
[0058] The performance tests similar to those of Example 1 were conducted on the produced
diurea grease. The results are shown in Table 1.
Comparative Example 5
[0059] 30.5 g of diphenylmethane-4, 4′-diisocyanate were charged into 450 g of mineral oil
having a viscosity at 100°C of 10.3 cSt, and were heated to 60°C so as to be uniformly
dissolved therein. 24.1 g of cyclohexylamine were added to the solution and agitated
vigorously. A gel-like substance was formed immediately. This substance was maintained
at 100°C for 30 minutes under continued agitation and admixed with 5.0 g of an anti-oxidant.
The resulting mixture was agitated thoroughly and passed through a roll mill. Separately,
21.2 g of tolylene diisocyanate were charged into 445 g of the same mineral oil and
dissolved therein. 24.2 g of cyclohexylamine were added to the solution and agitated
vigorously. A gel-like substance produced immediately was maintained at 100°C for
30 minutes under continued agitation and passed through a roll mill. The two produced
greases were agitated together uniformly to produce a grease composition.
The diurea composition was formed by 50 mol percent of a diurea compound represented
by the formula

and 50 mol percent of a diurea compound represented by the formula

[0060] The contents in the composition of the thickener formed by the diurea compounds were
10 wt.%.
[0061] The performance tests similar to those of Example 1 were conducted on the produced
diures grease. The results are shown in Table 1.
[0062] As may be seen from the results of the performance evaluation tests shown in Table
1, the diurea grease composition of the present invention has an improved shearing
stability and a high dropping point while being subject to small oil separation and
exhibiting superior thickening properties. On the other hand, the grease compositions
of the Comparative Examples 1 to 5 are equivalent or inferior to the inventive grease
composition in shearing stability and dropping point while being evidently inferior
to the inventive grease in thickening properties and oil separation at higher temperatures.
In the light of the above, the grease composition of the present invention is superior
in its various properties to the compositions of the Comparative Exmples 1 to 5.
Table 1
|
Thickener Contents (wt.%) |
ASTM Consistency |
Dropping Point °C |
Oil Separation (150°C, 200h) wt.% |
|
|
UW |
60W |
10⁵W |
|
|
Ex. 1 |
10 |
250 |
253 |
299 |
275 |
2.5 |
Ex. 2 |
10 |
265 |
266 |
301 |
282 |
3.2 |
Ex. 3 |
10 |
255 |
259 |
285 |
291 |
1.7 |
Ex. 4 |
10 |
242 |
247 |
288 |
282 |
0.6 |
Ex. 5 |
10 |
247 |
253 |
290 |
295 |
1.5 |
Ex. 6 |
10 |
271 |
275 |
325 |
261 |
4.6 |
Ex. 7 |
10 |
251 |
259 |
331 |
255 |
5.1 |
Ex. 8 |
10 |
284 |
287 |
342 |
271 |
2.7 |
Ex. 9 |
10 |
291 |
296 |
363 |
258 |
0.9 |
Ex. 10 |
10 |
266 |
289 |
305 |
285 |
3.8 |
Ex. 11 |
10 |
289 |
293 |
348 |
254 |
5.4 |
Comp. Ex. 1 |
10 |
326 |
315 |
199 |
249 |
10.7 |
Comp. Ex. 2 |
15 |
379 |
382 |
423 |
276 |
5.8 |
Comp. Ex. 3 |
10 |
358 |
357 |
371 |
277 |
7.2 |
Comp. Ex. 4 |
10 |
364 |
367 |
421 |
265 |
11.3 |
Comp. Ex. 5 |
10 |
372 |
374 |
433 |
255 |
12.1 |