BACKGROUND OF THE INVENTION
[0001] This invention relates to a synthetic ester base stock and, in particular, to a synthetic
ester base stock formed from an acid mixture having a high content of branched chain
acid, and a lubricant from the base stock having increased viscosity at elevated temperatures
and a decreased tendency to form deposits in high temperature uses.
[0002] Synthetic ester base stocks for use as chain oils and lubricants for gas turbine
engines are well known. The base stocks are combined with standard lubricant additive
packages to form the lubricant. In order for the lubricant to have properties suitable
for such high temperature use, the base stock must have certain physical properties.
For example, it is a requirement that the lubricant for turbine oils meet the specifications
set forth in military specification MIL-L-23699D. Chain oils should have low deposition
properties at high temperatures, a viscosity of at least about 7.0 centistockes (cSt)
and a reasonably low pour point below its ambient storage temperature.
[0003] In general, synthetic high temperature lubricants use esters as a base stock. The
esters are formed by reacting a polyol, such as pentaerythritol, either monopentaerythritol
(MPE) and/or dipentaerythritol (DPE) or trimethylolpropane (TMP) with various acids,
both straight chain and branched. Japanese patent applications No. JP 55-105644 and
No. 55-157537 disclose a neopentyl polyol ester of iso-C
9 acid and a straight chain saturated acid having from 4 to 18 and 2-24 carbon atoms,
respectively, preferably 6 to 14 carbon atoms for air compressor oils. U.S. Patent
No. 4,826,633, issued on May 2, 1989 and owned by the assignee herein, is directed
to an ester base stock for a turbine oil formed by reacting MPE and/or TMP with an
acid mixture of straight chain C
5-C
10 acids and 5 to 40 weight percent branched chain C
7-C
10 acids. Lubricants formed from these esters have a decreased tendency to form deposits
and have acceptably low pour points without use of DPE.
[0004] Several other United States patents disclose additional types of esters. For example,
U.S. Patent No. 3,694,382, issued to Kleiman, et al. on September 26, 1972, discloses
an ester blend for use as a synthetic lubricant. The ester blend includes esters of
trimethylolpropane and dipentaerythritol formed from a mixture of aliphatic monocarboxylic
acids.
[0005] U.S. Patent No. 4,049,563, issued to Burrous on September 20, 1977, discloses a jet
engine oil consisting of an ester of a C
4-C
12 monocarboxylic acid, a polyol selected from pentaerythritol, dipentaerythritol, tripentaerythritol,
trimethylolpropane, trimethylolmethane, trimethylolbutane, neopentylglycol and mixtures
thereof and a soluble methyl phenyl polysiloxane.
[0006] U.S. Patent No. 4,064,058, issued to Walker on December 20, 1977, discloses a grease
base stock including a blend of a normally liquid pentaerythritol ester product and
a neopentyl glycol ester product.
[0007] U.S. Patent No. 3,360,465, issued to Warman on December 26, 1967, discloses synthetic
ester lubricant compositions of pentaerythritol mixed esters. The pentaerythritol
utilized includes at least 1.5 weight percent dipentaerythritol. The acid includes
a mixture of from two to six monocarboxylic alkanoic acids having from five to nine
carbon atoms with some of the lower acids being branched chain.
[0008] Lubricant compositions containing pentaerythritol esters are also disclosed in EP-A-0
458 584 and EP-A-0 498 152.
[0009] Every lubricant has a characteristic tendency to form deposits when used in high
temperature applications such as an engine or on industrial oven chains. If the deposits
are excessive they will detract from the operating efficiency of the device and create
other problems such as filter plugging in engines or track jumping of chains.
[0010] Accordingly, it is desirable to provide a synthetic lubricant base stock which provides
lubricants having acceptable high temperature viscosity properties with improved resistance
to formation of carbon deposits when used in high temperature applications.
SUMMARY OF THE INVENTION
[0011] Generally speaking, in accordance with the invention, an improved synthetic ester
base stock is prepared by reacting at least one neopentyl polyol of the type defined
in claim 1 below, with a monocarboxylic acid mixture including at least one C
5-C
10 normal alkanoic acid and between 60 and 90 weight percent of C
7-C
10 branched chain acid, based on the total weight of the acid charged. The polyol is
a commercially available technical pentaerythritol. The straight chain monocarboxylic
acids include those having between 5 and 10 carbon atoms, such as valeric acid (pentanoic
acid), caproic acid (hexanoic acid), oenanthic acid (heptanoic acid), caprylic acid
(octanoic acid), pelargonic acid (nonanoic acid), capric acid (decanoic acid) and
mixtures thereof. The branched chain acid is preferably iso-C
9 acid, iso-nonanoic acid. When mixed with a standard lubricant additive package the
synthetic ester base stock prepared in accordance with the invention provides a lubricant
having a viscosity at 98.9°C (210° F.) of at least 7.0 centistokes and remains cleaner
at high chain oil operating temperatures than conventional chain oils.
[0012] Accordingly, it is an object of the invention to provide an improved synthetic ester
base stock.
[0013] Another object of the invention is to provide an improved synthetic ester base stock
having a decreased tendency to form deposits when used in a high temperature environment.
[0014] A further object of the invention is to provide an improved synthetic ester base
stock for high temperature applications and with a suitably higher viscosity.
[0015] Yet another is to provide a synthetic ester base stock with higher oxidative stability.
[0016] Still another object of the invention is to provide a synthetic ester base stock
which when combined with a standard lubricant additive package provides a lubricant
with a viscosity at 98.9°C (210° F.) of at least 7.0 centistokes and a pour point
of less than -23°C (-10°F).
[0017] Still another object of the invention is to provide the use of a synthetic ester
lubricant base stock as defined in claim 10 appended hereto as a high temperature
chain oil lubricant base stock.
[0018] Still other objects and advantages of the invention will in part be obvious and will
in part be apparent from the specification.
[0019] The invention accordingly comprises a composition of matter possessing the characteristics,
properties and the relation of components which will be exemplified in the composition
hereinafter described, and the scope of the invention will be indicated in the claims.
[0020] The synthetic lubricant base stock prepared in accordance with the invention is to
be used with standard lubricant additive packages. The lubricant base stock is the
reaction product of a neopentyl polyol as defined in the claims and a monocarboxylic
acid mixture having a high branched chain acid content, preferably between about 60-90
weight percent of a branched chain acid, based on the total acid charge. When the
base stock is mixed with a standard lubricant additive package, the lubricant has
a viscosity at 98.9°C (210°F) of at least 7.0 centistokes and a pour point of less
than -23°C (-10°F).
[0021] The neopentyl polyol comprises monopentaerythritol, C
5H
12O
4 (MPE, CAS #=115-77-5) which is a colorless solid with melting point of 255°-259°C;
and dipentaerythritol, C
10H
22O
7 (DPE, CAS #=126-58-9) which is a colorless solid having a melting point of 215°-218°C;
the commercially available technical grade pentaerythritol which is used in accordance
with the invention including monopentaerythritol and typically between about 6 to
15 weight percent dipentaerythritol. In the preferred embodiments of the invention,
the polyol is technical grade PE which includes about 12 weight percent DPE.
[0022] The acid component is monocarboxylic and includes at least one straight chain acid
having 5 to 10 carbon atoms and a branched chain acid having from 7 to 10 carbon atoms.
The branched chain acid preferably has nine carbon atoms, namely, iso-nonanoic acid.
Suitable straight chain acids include, but are not limited to, valeric acid, oneanthic
acid, caprylic acid, pelargonic acid and capric acid. Preferably, the straight chain
acid component is valeric (C
5) or is a mixture of heptanoic (C
7) and caprylic-capric (C
8-C
10). The caprylic-capric acid is identified as having between 8 and 10 carbon atoms,
but actually includes C
6 to C
12 acids and is substantially free of C
12 acid (less than 1%).
[0023] The amount of the preferred heptanoic and caprilic-capric mixture straight chain
acid component suitable for use in preparing esters in accordance with the invention
may vary widely. For example, the mixture may be from 30 to 70 weight percent heptanoic
acid and the balance the caprylic-capric mixture. In a preferred embodiment, the normal
acid mixture is 40-60 parts by weight of heptanoic acid and the balance caprylic-capric
acids.
[0024] The branched chain acid may be iso-C
7 acid, iso-C
8 acid, iso-C
9 acid or iso-C
10 acid. Preferably, the branched chain acid used is the iso-C
9 acid or iso-nonanoic acid, specifically known as 3,5,5-trimethylhexanoic acid (3,5,5-trimethylhexanoic
acid CAS # = [03302-10-1]). As used herein, iso-C
9 or iso-nonanoic acid is 3,5,5-trimethylhexanoic acid and has the formula:

Addition of the iso-nonanoic acid provides the necessary viscosity characteristics
and improves the pour point characteristics of the base stock and improves the oxidative
stability and deposition tendency.
[0025] The iso-acids other than iso-nonanoic can be used to provide base stocks which are
suitable for turbine engine or chain lubricant applications. For example, iso-C
7, iso-C
8 and iso-C
10 acids are available, but these acids contain a complex mixture of isomers, unlike
iso-C
9 acid which is mainly 3,5,5-trimethylhexanoic acid. The physical properties of an
acid that is a complex mixture of isomers can change if the relative ratios of the
isomeric components change and this affects the properties of an ester produced from
the acid. Therefore, to produce a consistent ester product, it is preferable to use
raw materials that consist of a single, high purity component, namely, iso-C
9 or iso-nonanoic acid.
[0026] The acid mixture is present in the reaction in an excess of about 5 to 10 weight
percent for the amount of the polyol mixture used. The excess acid is used to force
the reaction to completion. The excess acid is not critical to carrying out the reaction
except that the smaller the excess, the longer the reaction time. After the reaction
is complete, the excess acid is removed by stripping and refining. Generally, the
esterification reaction is carried out in the presence of conventional catalysts.
For example, a tin or titanium based catalyst of such a catalyst may be used. Tin
oxalate is an example.
[0027] Lubricants including ester base stocks prepared in accordance with the invention
are prepared by mixing a conventional additive package to the base stocks in conventional
concentrations. Typical additive packages are described in U.S. Patent Nos. 4,124,513,
4,141,845 and 4,440,657. The two former patents describe additive packages based on
an alkylphenyl or alkarylphenyl naphthylamine, a dialkyldiphenylamine, a polyhydroxy
anthraquinone, a hydrocarbyl phosphate ester with an S-alkyl-2-mercaptobenzotriazole
or an N-(alkyl)-benzothiazole-2-thione. The third patent describes additives of a
selected tertiarybutylphenyl substitute phosphate and a selected alkyl amine.
[0028] The invention will be better understood with reference to the following examples.
All percentages are set forth in percent by weight. These examples are presented for
purposes of illustration only and are not intended to be construed in a limiting sense.
Examples 1-12
[0029] A variety of ester base stocks were prepared. In each of the following runs the raw
materials identified in the Table and a tin oxalate catalyst were charged to a stirred
reactor capable of attaining 238°-254°C (460°-490° F). and a vacuum of at least 736.6
mm (29 inches) of mercury. The reactor was provided with a nitrogen sparge or blanket.
The charge was heated to a reaction temperature between about 226.7° and 232.2° (440°
and 450° F.) and the water of reaction was collected in a trap while the acids were
returned to the reactor. As reflux slowed, vacuum was applied in order to maintain
a reasonable reflux rate. When the hydroxyl value was reduced to a sufficiently low
level (a maximum of 5.0 mg KOH/gm), the bulk of the excess acid was removed by distillation
at the reaction temperature and maximum vacuum. The residual acidity was removed by
treatment with lime and water. The resulting ester base stock was dried and filtered.
[0030] The viscosity at 98.9°C (210° F.) was determined in accordance with ASTM D-445 for
each sample base stock together with the pour point in accordance with ASTM D-97.
TABLE I
| Table Run |
| RAW MATERIAL |
1 |
2 |
3 |
4 |
5 |
| Tech PE |
17.1 |
17.8 |
14.8 |
-- |
15.3 |
| Mono PE |
-- |
-- |
-- |
14.4 |
-- |
| Di PE |
-- |
-- |
-- |
-- |
-- |
| Valeric |
-- |
12.2 |
-- |
-- |
-- |
| Heptanoic |
12.4 |
-- |
-- |
-- |
-- |
| Caprylic-Capric |
12.4 |
-- |
-- |
-- |
-- |
| Isononanoic |
58.1 |
70.0 |
42.6 |
42.8 |
59.3 |
| Dodecanoic |
-- |
-- |
42.6 |
42.8 |
25.4 |
| PHYSICAL PROPERTIES |
|
|
|
|
|
| Viscosity @ 98.9°C (210°F), cSt |
8.91 |
9.9 |
10.1 |
9.51 |
10.6 |
| Viscosity Index |
114 |
97 |
129 |
128 |
110 |
| Pour Point, °C (°F) |
-42.8 (-45) |
-34.4 (-30) |
|
|
-37.2 (-35) |
| Freeze Point, °C (°F) |
|
|
-1.1* (+30) |
15.5* (+60) |
|
| * Product Crystallizes at Room Temperature; Freeze point data are approximate since
some liquid remains |
[0031] Lubricants prepared in accordance with the invention have a decreased tendency to
form deposits when used in high temperature applications. This reduced tendency was
demonstrated by mixing base stock with an additive package as follows:
Additive Package For Panel Test Work
[0032]
| Component |
Parts by Weight |
| Base Stock |
100 |
| Tricresyl Phosphate |
2.0 |
| p,p'-Dioctyl-diphenylamine |
1.0 |
| Octylphenyl-α-naphthylamine |
1.0 |
| Benzotriazole |
0.05 |
[0033] This additive package was selected as the standard package for comparing base stocks
in the panel test.
[0034] In this bench panel test, a stainless steel panel is electrically heated by means
of two heaters which are inserted into holes in the panel. The temperature is monitored
by means of a thermocouple. The panel is placed on a slight incline and heated to
282.2°C (540° F.) The lubricant to be tested is dropped onto the heated panel and
the characteristics are observed. The lubricant contacts the panel near the top of
the incline and is observed as a central dark band. The lubricant then tends to thin
out as it travels towards the lower end of the heated panel. It is along the oil-air-metal
interface that the degradation of the lubricant is best observed.
[0035] The results of the panel test for compositions prepared in accordance with the composition
of Run 1-2 of the Example showed little degradation along the oil-air-metal interface.
These lubricants are an ester mixture formed by reacting technical grade pentaerythritol
with an acid mixture including valeric or heptanoic and capric-caprylic as the normal
acid and iso-nonanoic acids.
[0036] Runs 3-5 were lubricants formed from base stocks prepared by reacting technical grade
PE or MPE and dodecanoic acid consistent with Runs 5 and 6 of Example 1 in JP 55-105644.
The panel test results for a lubricant made from these esters formed from dodecanoic
acid showed significantly increased carbonization along the oil-air-metal interface
compared to Runs 1-2.
[0037] By preparing an ester from technical grade pentaerythritol and an acid mixture of
a C
5-C
10 straight chain acid and a high iso- C
7 to C
10 acid content, synthetic ester lubricants having improved properties may be obtained.
The lubricants have improved oxidation stability with lower depositing tendency at
high temperatures, a viscosity at 98.9°C (210°F) of at least 7.0 cSt and improved
pour points. Preferably, the iso-acid is iso-C
9 acid and is present from 60 to 90 weight percent of the total acid charge. Thus,
the straight chain acid will be present from 10 to 40 weight percent of the acid charge
which maintains good pour point characteristics and an improved viscosity index. When
linear acids above C
10 are used, the resulting esters tend to crystallize at ambient temperatures. When
linear acids having less than five carbon atoms are used, odor and corrosion problems
arise.
1. A synthetic ester lubricant base stock, comprising the reaction product of:
a technical grade of pentaerythritol which is a mixture of monopentaerythritol and
between about 6 and 15 weight percent dipentaerythritol; and
an acid mixture including (1) at least one straight-chain acid having between 5 and
10 carbon atoms and (2) an iso-acid selected from the group consisting of iso-C7 acid, iso-C8 acid, iso-C9 acid, iso-C10 acid and mixtures thereof;
the iso-acid being present in an amount of from 60 to 90 percent by weight of the
acid mixture;
and
the resulting mixture of esters when admixed with a synthetic ester lubricant additive
package having a viscosity at 98.9°C (210°F) of at least 7.0 centistokes.
2. The synthetic ester lubricant base stock of Claim 1, wherein the iso-acid is iso-nonanoic
acid.
3. The synthetic ester lubricant base stock of Claim 1, wherein the iso-C9 acid is 3,5,5-trimethylhexanoic acid.
4. The synthetic ester lubricant base stock of Claim 2 wherein the straight-chain acid(s)
is/are a mixture of heptanoic acid (C7) and caprylic-capric acid (C8-C10).
5. The synthetic ester lubricant base stock of Claim 4 wherein the C7 and C8-C10 straight-chain acids are present in about equal amounts by weight.
6. The synthetic ester lubricant base stock of Claim 5 wherein the iso-nonanoic acid
is present from 65 to 75% by weight of the acid mixture.
7. The synthetic ester lubricant base stock of Claim 2 wherein the normal acid is valeric
acid.
8. The synthetic ester lubricant base stock of Claim 1, admixed with an effective amount
of a synthetic ester lubricant additive package for improving the high temperature
properties and the load factor of a lubricant.
9. A synthetic ester lubricant base stock according to anyone of the preceding claims
wherein iso-nonanoic acid is present from 65% to 75% by weight of the acid mixture.
10. The use as a high temperature chain oil lubricant base of a synthetic ester lubricant
base stock as defined in any one of the preceding claims.
1. Synthetisches Esterschmiermittel-Grundeimsatzmaterial, das das Reaktionsprodukt des
folgenden umfaßt;
Pentaerythritol technischer Güte, das ein Gemisch von Monopentaerythritol und zwischen
ungefähr 6 und 15 Gew.-% Dipentaerythritol ist; und
ein saures Gemisch, das (1) zumindest eine geradkettige Säure mit zwischen 5 und 10
Kohlenstoffatomen und (2) eine Iso-Säure einschließt, die aus der Gruppe ausgewählt
ist, die aus Iso-C7-Säure, Iso-C8-Säure, Iso-C9-Säure, Iso-C10-Säure, und Mischungen hiervon ausgewählt ist;
wobei die Iso-Säure in einer Menge von 60 bis 90 Gew.-% des sauren Gemisches vorliegt;
und
das sich ergebende Gemisch von Estern, wenn es mit einem synthetischen Esterschmiermittel-Additiv-Paket
gemischt wird, eine Viskosität bei 98,9°C von zumindest 7,0 Centistoke aufweist.
2. Synthetisches Esterschmiermtttel-Grundeimsatzmaterial nach Anspruch 1,
bei dem die Iso-Säure Iso-Nonansäure ist.
3. Synthetisches Esterschmiermitte-Grundeimsatzmaterial nach Anspruch 1,
bei dem die Iso-C9-Säure 3,5,5-Trimethylhexansäure ist.
4. Synthetisches Esterschmiermittel-Grundeimsatzmaterial nach Anspruch 2,
bei dem die geradkettige Säure(n) ein Gemisch aus Heptansäure (C7) und Capryl-Caprin-Säure (C8 - C10) ist/sind.
5. Synthetisches Esterschmiermittel-Grundeinsatzmaterial nach Anspruch 4,
bei dem die geradkettigen C7 und C8 - C10-Säuren bezogen auf das Gewicht in ungefähr gleichen Mengen vorliegen.
6. Synthetisches Estzerschmiermittel-Grundeinsatzmaterial nach Anspruch 5,
bei dem die Iso-Nonansäure von 65 bis 75 Gew.-% des sauren Gemisches vorliegt.
7. Synthetisches Esterschmiermittel-Grundeinsatzmaterial nach Anspruch 2,
bei dem die Normalsäure Valeriansäure ist.
8. Synthetisches Esterschmiermittel-Grundeinsatzmaterial nach Anspruch 1,
das mit einer wirksamen Menge eines synthetischen Esterschmiermittel-Additiv-Paketes
zur Verbesserung der Hochtemperatur-Eigenschaften und des Belastungsfaktors eines
Schmiermittels vermischt wird.
9. Synthetisches Esterschmiermittel-Grundeinsatzmaterial nach einem der vorhergehenden
Ansprüche,
bei dem Iso-Nonansäure von 65 bis 75 Gew.-% des sauren Gemisches vorliegt.
10. Verwendung als Hochtemperatur-Kettenölschmiermittel-Grundlage eines synthetischen
Esterschmiermittel-Grundeinsatzmaterials, wie in einem dar vorhergehenden Ansprüche
definiert.
1. Base lubrifiante d'ester synthétique comprenant le produit de la réaction de:
un pentaérythritol de qualité technique qui est un mélange de monopentaérythritol
ayant entre 6 et 15 % en poids de dipentaérythritol; et
un mélange d'acides comprenant (1) au moins un acide à chaîne droite ayant entre 5
et 10 atomes de carbone et (2) un iso-acide choisi dans le groupe consistant en iso-C7 acide, iso-C8 acide, iso-C9 acide, iso-C10 acide et des mélanges de ceux-ci;
l'iso-acide étant présent en une quantité de 60 à 90% en poids du mélange d'acides;
et
le mélange résultant d'esters lorsqu'il est mélangé avec un d'additif lubrifiant d'ester
synthétique ayant une viscosité à 98,9°C (210°F) d'au moins 7.0 centistokes.
2. La base lubrifiante d'ester synthétique de la revendication 1 dans lequel l'iso-acide
est l'acide isononanoïque.
3. La base lubrifiante d'ester synthétique de la revendication 1 dans lequel l'iso-C9 acide est l'acide 3,5,5-triméthylhexanoïque.
4. La base lubrifiante d'ester synthétique de la revendication 2 dans lequel les acides
à chaîne droite est/sont un mélange d'acide heptanoïque (C7) et d'acide caprylique-caprique (C8-C10).
5. La base lubrifiante d'ester synthétique de la revendication 4 dans lequel le ou les
acide(s) en C7 et C8-C10 à chaîne droite est/sont présent(s) en quantités environ égales en poids.
6. La base lubrifiante d'ester synthétique de la revendication 5 dans lequel l'acide
iso-nonanoïque est présent en 65 à 75% en poids du mélange d'acides.
7. La base lubrifiante d'ester synthétique de la revendication 2 dans lequel l'acide
normal est l'acide valérique.
8. La base lubrifiante d'ester synthétique de la revendication 1 mélangé avec une quantité
efficace d'additif de lubrifiant d'ester synthétique pour améliorer les propriétés
à température élevée et le facteur de charge d'un lubrifiant.
9. La base lubrifiante d'ester synthétique selon l'une quelconque des revendications
précédentes dans lequel l'acide iso-nonanoïque est présent en 65 à 75% en poids du
mélange d'acides.
10. L'utilisation d'une base lubrifiante d'huile de chaîne de haute température d'un base
lubrifiante d'ester synthétique telle que définie selon l'une quelconque des revendications
précédentes.