U.S. patent number 3,903,003 [Application Number 05/448,603] was granted by the patent office on 1975-09-02 for lubricating compositions containing an amido-amine reaction product of a terminally carboxylated isoprene polymer.
This patent grant is currently assigned to Shell Oil Company. Invention is credited to Zatis L. Murphy, Roland T. Schlobohm.
United States Patent |
3,903,003 |
Murphy , et al. |
September 2, 1975 |
Lubricating compositions containing an amido-amine reaction product
of a terminally carboxylated isoprene polymer
Abstract
Lubricating oil compositions for internal combustion engines
comprise a lubricant modified with an amido amine reaction product
formed between certain carboxylated hydrogenated polyisoprenes and
certain polyamines, imines (or "poly") and hydroxyl alkyl
polyamines.
Inventors: |
Murphy; Zatis L. (St. Louis,
MO), Schlobohm; Roland T. (Bethalto, IL) |
Assignee: |
Shell Oil Company (Houston,
TX)
|
Family
ID: |
23780953 |
Appl.
No.: |
05/448,603 |
Filed: |
March 6, 1974 |
Current U.S.
Class: |
508/507; 508/554;
525/333.1 |
Current CPC
Class: |
C08C
19/36 (20130101); C10M 133/56 (20130101); C08G
81/024 (20130101); C10M 2207/146 (20130101); C10M
2219/044 (20130101); C10N 2070/02 (20200501); C10M
2215/042 (20130101); C10M 2219/046 (20130101); C10M
2217/06 (20130101); C10M 2229/04 (20130101); C10M
2207/262 (20130101); C10M 2223/045 (20130101); C10M
2207/024 (20130101); C10M 2205/06 (20130101); C10M
2207/144 (20130101); C10N 2010/04 (20130101); C10N
2040/02 (20130101); C10M 2215/26 (20130101); C10M
2229/041 (20130101); C10N 2040/08 (20130101); C10M
2205/04 (20130101); C10M 2217/046 (20130101); C10M
2215/04 (20130101); C10M 2229/044 (20130101); C10M
2209/084 (20130101); C10M 2209/104 (20130101); C10M
2229/043 (20130101) |
Current International
Class: |
C10M
133/56 (20060101); C08C 19/36 (20060101); C08C
19/00 (20060101); C08G 81/02 (20060101); C08G
81/00 (20060101); C10M 133/00 (20060101); C10M
001/32 () |
Field of
Search: |
;252/51.5A
;260/93.5A |
References Cited
[Referenced By]
U.S. Patent Documents
|
|
|
2996455 |
August 1961 |
Brown et al. |
3642633 |
February 1972 |
Eckert et al. |
3761458 |
September 1973 |
Holler et al. |
3772196 |
November 1973 |
St. Clair et al. |
3816314 |
June 1974 |
Pappas et al. |
|
Primary Examiner: Gantz; Delbert E.
Assistant Examiner: Metz; Andrew H.
Claims
We claim as our invention:
1. A lubricating composition comprising a major proportion of a
lubricating oil and 0.1-10% by weight, sufficient to raise the
viscosity index and impart detergency to the oil of a halogen-free
nitrogen-containing amido amine reaction product of a terminally
carboxylated substantially completely hydrogenated polyisoprene
containing less than 2% of the original olefinic unsaturation and
having an average molecular weight between about 20,000 and 250,000
and a nitrogen compound of the group consisting of polyalkylene
amines and hydroxy alkyl polyalkylene amines, said reaction product
resulting from heating the hydrogenated carboxylated polyisoprene
and nitrogen compound for 15-480 minutes at
175.degree.-250.degree.C.
2. A composition according to claim 1 wherein the reaction product
is formed between monocarboxylated hydrogenated polyisoprene and a
pentaethylene hexamine.
3. A composition according to claim 1 wherein the reaction product
is formed between monocarboxylated hydrogenated polyisoprene and a
hydroxy ethyldiethylene triamine.
4. A composition according to claim 1 wherein the carboxylated
hydrogenated polyisoprene has an average molecular weight between
about 23,000 and 80,000 and the nitrogen compound has an average
molecular weight between about 150 and 1800.
5. A composition according to claim 1 containing in addition a
power point depressing amount of a polymethacrylate.
Description
BACKGROUND OF THE INVENTION
This invention relates to novel lubricating compositions containing
a critically defined block copolymer imparting to the compositions
increased viscosity, viscosity index and detergency. The lubricants
are especially useful in internal combustion engines but may be
employed for other related purposes such as in transmission fluids,
gear lubricants and the like.
DESCRIPTION OF THE PRIOR ART
The art of lubricating oil formulation has become increasingly
complex with the ever more stringent demands made by the developing
automotive technology. One of the primary requirements is to
provide an economical lubricant which may be utilized over a wide
range of operating conditions, especially insofar as temperature
variations are concerned. At the same time, the formulated
lubricant should also possess an ability to withstand oxidative
influences and, if possible, impart detergency and dispersancy
during its use as well as during storage. Multi-grade lubricants
are becoming virtually a necessity in this field.
By "multi-grade lubricants" is meant lubricants which meet a
0.degree.F viscosity specification and a 210.degree.F viscosity
specification, such as is shown for motor oils by the following
table derived from SAE, J300a taken from the SAE Handbook for
1969:
SAE SAE Oil Viscosity at Oil Viscosity at Grade Spec. 0.degree.F,
poises Grade Spec. 210.degree.F, SUS
______________________________________ -- -- 20 45-58 5W 12 maximum
30 58-70 10W 12-24 40 70-85 20W 24-96 50 85-110
______________________________________
According to the table, for example, an SAE 10W/50 oil must have a
viscosity at 0.degree.F between 12 and 24 poises and a viscosity at
210.degree.F of between 85 and 110 SUS.
The art has evolved a number of multi-grade oils such as SAE 10W/30
and SAE 20W/40 oils but with few exceptions has not been able to
formulate wider multi-grade oils such as SAE 10W/50 having low oil
consumption and high shear stability. Commercially, such
formulations should be economically feasible, capable of large
scale production, versatile in regard to the base stock and
preferably resistant to degradation under conditions of high
shear.
A large variety of polymeric additives have been employed primarily
as thickening agents, viscosity index (VI) improvers and pour point
depressants. A common limitation of essentially all of these is
shear sensitivity. This is not unexpected, since most of these
polymers are relatively high molecular weight materials, and
consequently are readily subject to shear degradation. On the other
hand, relatively low molecular weight polymeric materials, at least
up to the present time, have proven to be relatively ineffective as
thickeners or VI improvers in automotive engine lubricants, even
though they may have reasonably good shear stability.
A number of polymeric additives having a certain polarity have been
suggested as lubricating oil additives. These include, for example,
polymers shown as sludge dispersants in U.S. Pat. No. 2,838,456. In
this patent, reference is made to graft copolymers wherein a polar
monomer is grafted onto a polymer of an isoolefin or a diene. Not
only is the polymer left in a non-hydrogenated state (and therefore
susceptible to oxidation) but also the proportion of the polar
monomer employed was so high as to seriously reduce oil solubility
of the graft copolymer.
Two other patents of related subject matter are U.S. Pat. Nos.
2,965,571 and 3,378,492. Each of these teaches the use of certain
graft copolymers but in neither case is reference made to
hydrogenated polymers or to polymers having only a low proportion
of the polar graft material such as acrylates or acrylonitrile.
OBJECTS OF THE INVENTION
It is an object of the present invention to provide improved
lubricating compositions. It is another object of the invention to
provide improved multi-grade lubricants. It is a particular object
of the invention to provide high viscosity index lubricating
compositions exhibiting detergency and dispersancy characteristics.
Other objects will become apparent during the following detailed
description of the invention.
STATEMENT OF THE INVENTION
Now, in accordance with the present invention, lubricating
compositions are provided comprising a major proportion of a
lubricating oil and 0.1-10% by weight of the halogen-free
nitrogen-containing amido amine reaction product of a terminally
carboxylated substantially completely hydrogenated polyisoprene
having an average molecular weight between about 20,000 and 250,000
and a nitrogen compound of the group consisting of polyalkylene
amines (sometimes referred to as polyalkylene imines) and hydroxyl
polyalkylene amines.
DESCRIPTION OF THE PREFERRED EMBODIMENTS
In accordance with this invention, it has been found that the amido
amine reaction products to be described more fully hereinafter, not
only increase the viscosity of hydrocarbon oils but also increase
the viscosity index thereof and provide detergency and dispersancy
properties. Furthermore, these reaction products are stable with
respect to oxidation and shear.
The percursors of the polymeric additives are preferably formed by
polymerization of isoprene using a lithium-base initiator,
preferably a lithium alkyl in an inert solvent medium predominating
in hydrocarbons under conditions known in the art to produce a
polyisoprene referred to as a "living polymer" wherein the growing
end of the polymer chain is associated with a lithium radical. This
living polymer is then subjected to carboxylation such as by
reaction with carbon dioxide to form a polyisoprene bearing a
terminal carboxyl group.
The carboxylated polymer is then subjected to hydrogenation under
conditions leading to substantially complete reduction of all
aliphatic unsaturation. "Substantially complete" means
hydrogenation to an extent sufficient to reduce at least about 98%
of the olefinic unsaturation and preferably higher than about 99%
thereof. Hydrogenation is preferably effected by the use of
catalysts which are the reaction products of a nickel or cobalt
carboxylate and a halogen-free organo alkene compound, preferably
an aluminum trialkyl. The temperature of hydrogenation may vary
from about room temperature to about 175.degree.C for times from
about 1 minutes to 4 hours. Hydrogenation is normally conducted in
a saturated hydrocarbon medium and may be carried out in a batch
operation in an autoclave or in a continuous process utilizing
trickle phase techniques, for example.
While the average molecular weight of the polyisoprene component
may vary over a wide range, it is preferred that it lie between
about 21,500 and 250,000, still more preferably between about
23,000 and 80,000.
The nitrogen compounds utilized for the formation of the amido
amines of this invention may be polyalkylene amines, and hydroxy
alkyl polyalkylene amines as well as mixtures thereof. The term
"polyalkylene amine" is meant to include those polyamines having
the formula: ##EQU1## wherein x is an integer from 2 to about 10, R
is a hydrogen or a lower alkyl hydrocarbon substituent and
"alkylene" is a lower alkylene, i.e. divalent open chain
hydrocarbon group having from 1 to 8 carbon atoms. The hydroxy
alkyl polyalkylene amines are those in which the terminal hydrogen
atom in the above structural formula is replaced by a hydroxy alkyl
radical or a polyalkylene oxide, hydroxy terminated radical in
which the alkyl group has from 1 to 8 carbon atoms. Typical species
of reactants falling within the above-described group of compounds
are the following:
ethylene diamine
diethylene triamine
triethylene tetramine
tetraethylene pentamine
pentaethylene hexamine
polyethylene imine
hydroxyethyl diethylene triamine
poly(hydroxyalkyl) derivatives of ethylene diamine homologs
poly propoxylated pentaethylene hexamine
While it is possible to form these reaction products by converting
the carboxylated hydrogenated polyisoprene to its acryl chloride by
reaction with thionyl chloride and then by reaction with the
polyamine, this not only entails an extra process step, but also
inherently causes emulsification difficulties due probably to the
detergency properties of the resulting products. This becomes
especially evident during water washing of the reaction product for
the removal of hydrogen chloride or any amine hydrochlorides. Thus,
in accordance with the preferred aspect of this invention the amido
amine reaction products are directly prepared by reaction of the
carboxylated hydrogenated polyisoprene and one or more of the
above-described nitrogen-containing compounds. While little or no
reaction occurs at relatively lower temperatures such as
145.degree.C, it has been found that satisfactory rates of reaction
are experienced at temperatures in the order of 175.degree.C or
higher, preferably 185-250 in the presence of a lubricating oil if
desired or in bulk form. By this means when using a lubricating oil
medium for the reaction, a concentrate of the amido amine can be
conveniently prepared. Heating is continued for periods of time
which will vary with the reactants and temperature but it normally
will be between about 15 minutes and 8 hours. If the product is
prepared in the absence of a lubricating oil it may be recovered
for example by dissolving in toluene, washing with a lower alcohol
such a methanol and precipitating the product between addition of
still further alcohol.
The reaction products prepared as described above comprise a
hydrogenated polyisoprene segment connected by a single amido
linkage with the polyamine. It is preferred as referred to
hereinabove that the hydrogenated polyioprene segment have an
average molecular weight between about 23,000 and 80,000 and in
conjunction therewith that the nitrogen compound utilized to form
the amido amine have an average molecular weight between about 150
and 1800 although polyalkylene amines having average molecular
weights up to about 2,500 may in fact be used.
The oil component of the lubricating compositions according to the
present invention is especially designed for the preparation of
multi-grade lubricants although single grade lubricants may be
compounded as well. Still more specifically, the present
combination of block copolymer and pour point depressant is
especially beneficial in wax-containing lubricating oil cuts such
as found in Mid Continent oils, West Texas Ellenburger crudes, East
Texas crudes, Oklahoma crudes, Pennsylvania crudes and California
crudes and similar waxy crudes which may be referred to as paraffin
base crudes, naphthenic crudes or mixed based crudes as
distinguished from asphalt base crudes. While lubricating oils of
any viscosity may be used as the base for the present compositions,
the preferred oils are referred to as High Viscosity Index
Neutrals, such as HVI 100 Neutral, HVI 250 Neutral and HVI Bright
Stock as well as combinations of the same. The numerals before
"Neutral" are approximate viscosities at 100.degree.F in Saybolt
Universal Seconds. Also included in this general term HVI for the
purpose of this description, are very high viscosity index (VHVI)
oils such as those prepared via hydrocracking of poor quality oils,
such as low viscosity index (LVI) oils. More volatile oils may be
employed for special purposes such as (HVI) 80N. These neutral oils
are produced by well-known refining methods, such as distillation,
dewaxing, deasphalting, dearomatizing as by solvent extraction,
etc., as may be needed, dependent largely on the crude oil used.
Typical properties of these HVI oils are the following:
Properties of Base Oils HVI HVI HVI HVI VHVI
__________________________________________________________________________
Designation 80 N 100 N 250 N 150 BS 100 N VIS 210.degree.F (SUS)
38.0 39.8 50.0 157 38.6 VIS 100.degree.F (SUS) 82 107 265 2775 82.7
VI 103 93 93 95 126 Gravity (lbs/gal) 7.08 7.20 7.33 7.44 7.21 Pour
Point (.degree.F) 5 20 20 15 0 Flash Point (.degree.F) 360 405 430
575 400 Aniline Cloud Point (.degree.F) 203 213 220 260 226 %
Aromatics by UV 15 11 14 27-40 5 %w S .05 .09 .05 .16 .05 ASTM
Color L0.5 L0.5 L1.0 L4.5 L0.5
__________________________________________________________________________
EXAMPLE I
Polyisoprene was prepared in isopentane solution using secondary
butyllithium as the initiator to produce a polymer having an
average molecular weight of about 30,000. The living polymer was
carboxylated at about -40.degree.C by the use of carbon dioxide.
This was subjected to hydrogenation in the presence of a catalyst
comprising the reaction product of nickel octoate and aluminum
triethyl to form the hydrogenated carboxylated polymer.
The product was dissolved in xylene and reaction at 145.degree.C
was attempted with pentaethylene hexamine (PEHA). Little or no
reaction occurred at this temperature. However, when the
temperature was increased to 200.degree.C reaction occurred to form
a homogenous mixture after several hours. The cooled polymer was
dissolved in an excess of toluene and washed with methanol which
caused the product to precipitate free of unreacted polyamine. The
polymer was dissolved in toluene dried with sodium sulfate and the
solvent stripped off. The product characterized by the infra red
spectra and physical properties was shown to be the same as the
amido amines obtained by way of the intermediate acid chloride
reactant referred to hereinabove.
EXAMPLE II
In order to determine the dispersant properties of the two amido
amines prepared as described in Example I, the additives were
dispersed in a base blend and subjected to Micro Air Oxidation
Tests (MAOT). The base blend was as follows:
HVI 100 Neutral lube oil -- Methylene bis-(2,6-di-tert-butyl
phenol) 1% Alkyl zinc dithiophosphate 1% Highly overbased calcium
petroleum sulfonate 0.7%
The test was conducted at 350.degree.F with 4.2 liters of air per
hour in the presence of 20 ppm each of soluble iron and copper as
the metal naphthenates. The following table shows the results
obtained. The time of failure in this test is defined as the time
for first appearance of a center residue in a blotter spot using
Millipore blotter spot paper or Whatman blotter spot paper.
TABLE I ______________________________________ Additive %w Hours to
Fail ______________________________________ None -- <17 EP-PEHA*
4.2 >31<48 EP-HEDTA** 4.5 >31< 48
______________________________________ *amido amine of hydrogenated
carboxylated polyisoprene and pentaethylene hexamine **amido amine
of hydrogenated carboxylated polyisoprene and hydroxyethyl
diethylene triamine
It will be noted that the addition of the two amido amines
substantially improved the Micro Air Oxidation Test results over
that obtained with the base blend.
EXAMPLE III
Two of the amido amines of this invention were dispersed in 100 HVI
Neutral to determine their viscosity index effect. For comparison,
the hydrogenated carboxylated polyisoprene precursor was likewise
tested as was the unmodified lubricating oil. The following table
shows that the unmodified oil had a viscosity index of 93. In order
to increase the original 210.degree.F viscosity of the oil to 77
SUS, it was necessary to add 4.7% of the free carboxyl precursor.
In this concentration, the resulting oil had a viscosity index of
152. Both of the amido amines of this invention required
substantially less polymer to raise the 210.degree.F viscosity to
77 but in spite of this the resulting oils had substantially higher
viscosity indicies than that obtained with the oil contaning the
precursor.
TABLE II ______________________________________ Viscometric
Properties of HVI 100 Neutral (WR) Containing Block Polymers
Polymer Conc. (%w) 210.degree.F Vis., SUS VI
______________________________________ EP(30)-CO.sub.2 H 4.7 77 152
EP(30)-PEHA* 3.25 77 162 EP(30)-PEI** 3.85 77 172 None -- 39.5 93
______________________________________ *See footnote in Table I
**Amido amine of hydrogenated carboxylated polyisoprene and
polyethylene imine (1800 mol wt)
EXAMPLE IV
Sequence VC Engine Tests were performed on the following
lubricating oil composition:
Wt% ______________________________________ HVI 100N Lube Oil 83.0
Dimethyl silicone autifoam, 12, 500cs, ppm (10.0) Dispersant VI
Improver of this invention 2.0 Zinc dialkyl dithiophosphate 0.3
Mixed polymethacrylate 0.3 Isooctylphenoxytetramethoxyethanol 0.5
Basic Ca alkyl salicylate 3.8 ZnBis(octylphenyl)thionothiophosphate
2.3 Ca sulfonates 3.8 Polyisobutenyl succinimide of
tetraethylenepentamine 4.0
______________________________________
This lubricating oil had an SAE grade of 10W/40. The "Dispersant VI
Improver of this Invention", present in an amount of 2.0 wt.% was
the amido amine of hydrogenated carboxylated polyisoprene and
polyethylene imine, the respective average molecular weights of
each were 48,000 and 600. The following ratings were obtained and
are compared with specification limits.
TABLE III ______________________________________ Sequence VC
Results.sup.a Specification Limits
______________________________________ Average Sludge Deposits 9.2
8.5 min. Piston Skirt Varnish Deposits 8.4 7.9 min. Average Varnish
Deposits 8.0 8.0 min. ______________________________________ .sup.a
Rating (10 = clean).
* * * * *