[0001] The invention relates to dispersant additives and to fuel and lubricant compositions
containing them. In particular, it relates to certain amides made from polyamines,
monocarboxylic acid and polycarboxylic acid.
[0002] It is known that in the normal use of organic industrial fluids, such as lubricating
oils, transmission fluids, bearing lubricants, power transmitting fluids and the like,
oxidizing conditions are encountered which may result in the formation of sludge,
lacquers, corrosive acids and the like. These products are undesirable in that they
produce oxidation residues or heavy contaminants which may cause normal breakdown
of the fluid, leading eventually to severe damage to the parts of the equipment being
lubricated.
[0003] In the lubrication of modem engines, oil compositions must be able to prevent acids,
sludge and other solid contaminants from remaining near the moving metal parts. Poor
piston travel and excessive engine bearing corrosion may result unless the oil can
prevent sludge and oxidation products from depositing in the engine. Bearing corrosion
is another serious problem in gasoline engines which operate at an oil temperature
of about 149°C (300°F) or higher.
[0004] The most desirable way of decreasing the effect of these problems is to add to the
base organic fluid a detergent or dispersant additive capable of dispersing the solid
particles to prevent them from interfering with the normal operation of the equipment,
thereby leaving the metal surfaces relatively dean. Today, with modem equipment operating
under increasingly strenuous conditions, it is desirable to develop new detergents
which have improved dispersant properties, which are soluble in the fluid medium to
which they are added, and which are themselves stable therein.
[0005] U.S. Patent 3,714,045 discloses lubricant compositions containing lubricants and
a polyimide produced by reacting (1) a heteropolymer produced by reacting an olefin
with maleic anhydride in the presence of a free-radical initiator with (2) a primary
arylamine.
[0006] U.S. 3,936,
480 discloses the reaction of a polyal- kylenesuccinic acid anhydride with diphenylolpropane
of the formula I and tetraethylenepentamine, pyridine or triethyienetetramine. It
should be noted, however, that in all cases wherein diphenolpropane is reacted, a
catalyst is used. This is an absolute necessity when a phenolic OH is present, because
there will be no reaction with the anhydride without it
[0007] U.S. 3,868,330 discloses a lubricant or fuel composition containing an additive amount
of at least one oil-soluble high molecular weight compound made by chlorinating
(1) a mixture of a C50 monocarboxylic acid and a low molecular weight polycarboxylic acid, e.g., succinic
acid; or
(2) a mixture of a C50 ethyleneically unsaturated aliphatic hydrocarbon, a low molecular weight monocarboxcylic
acid and a low molecular weight polycarboxylic acid.
[0008] This invention provides a reaction product prepared by reacting (1) at least one
fatty monocarboxylic acid containing 10 to 20 carbon atoms, (2) at least one alkenyl-
or alkylsuccinic acid or anhydride, where the alkenyl group is derived from a mixture
of C" to C
26, preferably C
18 to C,., olefins and (3) at least one polyamine of the formula RNH[R
1NH]
x--H wherein R is a hydrocarbyl group containing 1 to 5 carbon atoms, R
1 is a C, to C, alkylene group and x is 1 to 9.
[0009] This invention also provides a process for making a dispersant for fuel and lubricating
compositions comprising reacting (1) at least one fatty monocarboxylic acid containing
10 to 20 carbon atoms, (2) at least one alkenyl- or alkylsuccinic acid or acid anhydride
where the alkenyl or alkyl group is derived from a mixture of C
12 to C
26 olefins and (3) at least one polyamine of the formula

wherein R and R
1 have the definitions given above.
[0010] The present invention further provides a lubricant or liquid fuel comprising a major
proportion of a lubricant or liquid fuel and a dispersant amount of a product obtained
by the process described hereinabove.
[0011] The preferred method of preparing the reaction products of this invention involves
reacting one of the two types of acids with the amine at from about 100°C to about
175°C, preferably about 150°C to about 175°C, then reacting this product with the
other acid at the same temperature.
[0012] The two types of acids will be used in such amounts that one type will supply from
about 30% to about 90% by weight of the required amount and the other type will supply
the complementary amount The quantity of polyamine will be chosen such that the acids
react therewith to form amide or imide groups with at least 40% by weight of the available
amino groups. Preferably from about 30% to about 60% of the amino groups are left
unreacted, but an effective dispersant is obtained when 60% of the amino groups is
reacted with the acid mixture.
[0013] Another method that can be used to form the product involves reacting the amine with
a mixture of the acids. The same temperature mentioned for the preferred method may
be used for both acid-amine reactions. Further, the final product is made by using
the same relative proportions of acid mentioned above, and the percentage of reacted
amino groups in a given product will be the same.
[0014] The useful fatty monocarboxylic acids have the formula

where R is a hydrocarbyl group containing 10 to 20 carbon atoms. Among the saturated
members covered by the formula are capric, lauric, myristic, palmitic, stearic and
arachidic and tall oil fatty acids. The unsaturated members include oleic, linoleic,
linolenic, eieostearic and ricinoleic acids.
[0015] The preferred polycarboxylic acids and anhydrides contemplated have the formula II
or III where R is an alkenyl or alkyl group derived from a mixture of C
18 to C,. monomers. Polyamines include triethylenetetramine, tetraethylenepentamine,
pentaethylenehexamine, etc. to nonaethylenedecamine, and the methylene, propylene,
butylene and amylene counterparts.
[0016] The additive compositions of the present invention impart valuable properties, as
hereinbefore indicated, to liquid hydrocarbon combustion fuels, including the distillate
fuels, i.e., gasolines and fuel oils. The fuel oils that may be improved in accordance
with the present invention are hydrocarbon fractions having an initial boiling point
of at least about 38°C (100°F) and an end-boiling point no higher than about 399°
(750°F), and boiling substantially continuously throughout their distillation range.
Such fuel oils are generally known as distillate fuel oils. It is to be understood,
however, that this term is not restricted to straight run distillate fractions. The
distillate fuel oils can be straight run distillate fuel oils, catalytically or thermally
cracked (including hydrocracked) distillate fuel oils, or mixtures of straight run
distillate fuel oils, naphthas and the like, with cracked distillate stocks. Moreover,
such fuel oils can be treated in accordance with well-known commercial methods, such
as, acid or caustic treatment, hydrogenation, solvent refining, clay treatment etc.
[0017] The distillate fuel oils are characterized by their relatively low viscosities, pour
points, and the like. The principal property which characterizes the contemplated
hydrocarbons, however, is the distillation range. As mentioned hereinbefore, this
range will lie between about 38°C (100°F) and about 399°C (750°F). Obviously, the
distillation range of each individual fuel oil will cover a narrower boiling range
falling, nevertheless, within the above-specified limits. Likewise, each fuel oil
will boil substantially continuously throughout its distillation range.
[0018] Contemplated among the fuel oils are Nos. 1, 2 and 3 fuel oils used for heating and
as diesel fuel oils, and the jet combustion fuels. The domestic fuel oils generally
conform to the specifications as set forth in A.S.T.M. Specifications D396-48T. Specifications
for diesel fuels are defined in A.S.T.M. Specification D975-48T. Typical jet fuels
are defined in Military Specification MIL-F-5624B.
[0019] The gasolines that are improved by the additive compositions for this invention are
mixtures of hydrocarbons having an initial boiling point falling between about 24°C
(75°F) and about 57°C (135°F) and an end-boiling point falling between about 121°C
(250°F) and about 232°C (450°F). As is well known in the art, motor gasoline can be
straight run gasoline or, as is more usual, it can be a blend of two or more cuts
of materials including straight run stock, catalytic or thermal reformate, cracked
stock, alkylated natural gasoline, and aromatic hydrocarbons. The concentration of
additive in the fuel will range from bout 0.00001% to about 0.1 % by weight of the
composition.
[0020] The additive is effective in lubricant compositions for the purposes disdosed in
ranges from about 0.1 % to about 10.0% by weight of the total lubricant composition.
Preferred is from about 1.0% to 5.0%. In general, the additives of this invention
may also be used in combination with other additive systems in conventional amounts
for their known purpose. The use of additive concentrations of borated alcohols in
premium quality automotive and industrial lubricants further improves upon such fluids'
fuel economy characteristics. The non-metallic compositions described herein are useful
at said moderate concentrations and do not contain any potentially undesirable phosphorus,
corrosive sulfur or metallic safts.
[0021] The lubricants contemplated for use herein include both mineral oil and synthetic
hydrocarbon or hydrocarboxy oils of lubricating viscosity, mixtures of mineral oils
and such synthetic oils, and greases prepared therefrom. The synthetic hydrocarbon
oils include long chain alkanes such as cetanes, and olefin polymers such as trimers
and tetramers of octene and decene. Such synthetic hydrocarbon oils can be mixed with
other synthetic oils, including (1) ester oils such as pentaerythritol esters of monocarboxylic
acids having 2 to 20 carbon atoms, (2) polyglycol ethers, and (3) polyacetals. Especially
useful among the synthetic esters are those made from polycarboxylic acids and monohydric
alclohols. More preferred are the ester fluids made from pentaerythritol, and an aliphatic
monocarboxylic acid containing from 1 to 20 carbon atoms, or mixtures of such acids.
[0022] The following example is offered as a specific illustration of the invention.
EXAMPLE
[0023] A mixture of 189g (1.0 mole) of tetraethylenepentamine and 712.5g (2.5 moles) of
tall oil fatty acids was heated to about 175°C and was stirred over a three hour period,
evolving 45.0 g (2.5 moles) of water. A typical tall oil fatty acid contains about
45-50% oleic acid, 45-50% linoleic acid and 1-6% rosin acids. Subsequently, 106 grams
(0.25 mole) of mixed C,, to C,, alkenylsuccinic anhydride derived from ethylene polymerization
were added and the mixture was stirred for one hour at 175°C under reduced pressure
to aid in the removal of water. The final product was obtained by filtration.
[0024] The deposit-forming tendencies of a fuel were determined in an 8-hour engine test.
This accelerated test, when run on fuels that contain no detergents, produces an amount
of deposit equivalent to the amount observed in 4.000 miles of operation in field
tests on taxicab fleets. In accomplishing the test, a Ford 4.9 liter (300 C.I.D.)
engine was equipped with notched rings to increase the amount of blowby and with a
glass throttle body section. The engine was operated for 8 hours, using the fuel under
test, at alternate idling and running cycles. In the idle cycle the engine was run
for 5 minutes at idling speed of 400 rpm with no load. Then for 1 minute the engine
was run at a speed of 2,500 rpm under a load of 30 BPH and a manifold pressure of
31.7 kPa (9.4 in. of mercury). During the running cycle the blowby and part of the
exhaust were released into the carburetor air intake during the idling cycle. After
8 hours of operation at alternate run and idle, the carburetor was examined and rated
for amount of deposit in the throttle throat The fuel used was a gasoline comprising
40% catalytically cracked component, 40% catalytically reformed component and 20%
alkylate, the overall mixture having a boiling range of about 35-210°C.
[0025] The results are shown in the following table.

1. A product formed by reacting (1) at least one fatty monocarboxylic acid containing
10 to 20 carbon atoms, (2) at least one alkenyl- or alkylsuccinic acid or acid anhydride
thereof, where the alkenyl or alkyl group is derived from a mixture of C" to C26 olefins and (3) at least one polyamine of the formula
RNH[R1NH]x--H
wherein R is a hydrocarbyl group containing 1 to 5 carbon atoms, R1 is a C, to C, alkylene group and x is 1 to 9.
2. The product of claim 1 wherein the fatty monocarboxylic acid is selected from capric, lauric, myristic,
palmitic, stearic, arachidic, oleic, linoleic, linolenic, eleostearic, ricinoleic
acids and mixtures thereof.
3. The product of any one of the preceding claims wherein the potyamine is selected
from triethylenetetramine, tetraethylenepentamine, pentaethylenedexamine, non- ethyienedecamine
and the methylene, propylene, butylene and amylene counterparts thereof.
4. The product of any one of the preceding claims wherein the alkenyi- or alkylsuccinic
acid or anhydride has the formula II or III where R is an alkenyl or alkyl group derived
from a mixture of C18 to C24 monomers.
5. The product of any one of the preceding claims wherein the fatty monocarboxylic
acid comprises between about 30 and about 90 percent by weight of the total amount
of monocarboxylic and alkenyl-, or alkylsuccinic acids or acid anhydride reacted.
6. The product of any one of the preceding claims wherein the quantity of polyamine
selected is one wherein at least 40% by weight of the available amino groups therein
are reacted with the acids.
7. The product of any one of the preceding claims wherein the reaction is conducted
by reacting one of acids (1) and (2) with amine (3) at a temperature of from 100°
to 175°C and then reacting this product with the other acid at the same temperature.
8. The product of any one of the preceding claims wherein the reaction is conducted
by reacting amine (3) with a mixture of acids (1) and (2) at a temperature of from
100°C to 175°C.
9. A process for making a dispersant for fuel and lubricating compositions comprising
reacting (1) at least one fatty monocarboxylic acid containing 10 to 20 carbon atoms,
(2) at least one alkenyl- or alkylsuccinic acid or acid anhydride, where the alkenyl
or alkyl group is derived from a mixture of C" to C,, olefins and (3) at least one
polyamine of the formula
RNH[R1NH]x--H
wherein R is a hydrocarbyl group containing 1 to 5 carbon atoms, R1 is a C, to C, alkylene group and x is 1 to 9.
10. The process of claim 9 wherein the fatty monocarboxylic acid is selected from
the group consisting of copric, lauric, myristic, palmitic, stearic, arachidic, oleic,
linoleic, linolenic, eleostearic, ricinoleic acids and mixtures thereof.
11. The process of any one of claims 9 & 10 wherein the polyamine is selected from
the group consisting of triethylenetetramine, tetraethylenepentamine, pentaethylenedexamine,
nonethylenedecamine and the methylene, propylene, butylene and amylene counterparts
thereof.
12. The process of any one of claims 9, 10 and 100 wherein the alkenyl- or alkytsuccinic
acid or anhydride has the formula II or III wherein R is an alkenyl or alkyl group
derived from a mixture of C18 to C24 monomers.
13. The process of any one of claims 9-12 wherein the fatty monocarboxylic acid comprises
between about 30 and about 90 percent by weight of the total amount of monocarboxylic
and alkenyl-, or alkylsuccinic acids or acid anhydride reacted.
14. The process of any one of claims 9-13 wherein at least 40% by weight of the polyamine
available amino groups therein are reacted with the acids.
15. The process of any one of claims 9-14 wherein the reaction is conducted by reacting
one of acids (1) and (2) with amine (3) at a temperature of from 100° to 175°C and
then reacting this product with the other acid at the same temperature.
16. The process of any one of claims 9-15 wherein the reaction is conducted by reacting
amine (3) with a mixture of acids (1) and (2) at a temperature of from 100° to 175°C.
17. A fuel conposition comprising a major proportion of a liquid fuel and a dispersant
amount of the product of any one of claims 1-8.
18. The fuel composition of claim 17 wherein the dispersant constitutes 0.00001% to
0.1% by weight of the composition.
19. A lubricant composition comprising a major proportion of a liquid lubricant and
a dispersant amount of the product of any one of claims 1-8.