[0001] The presently claimed invention is directed to the use of 2,5-furandicarboxylic acid
esters as lubricants and a process for their preparation. The 2,5-furandicarboxylic
acid esters are preferably obtained by reacting 2,5-furandicarboxylic acid with at
least one branched or linear, substituted or un-substituted aliphatic C6 to C20 alcohol.
[0002] The commercially available lubricant compositions are produced from a multitude of
different natural or synthetic components. To improve the required properties, according
to the field of use, further additives are usually added.
[0003] The various lubricants must satisfy extremely high criteria such as high viscosity
index, good rheological performance, particularly at extreme temperatures, high oxidation
stability, good thermal and hydrolytic stability and comparable properties.
[0004] Accordingly, high-performance lubricant oil formulations exhibit a special performance
profile with respect to shear stability, low-temperature viscosity, long service life,
evaporation loss, fuel efficiency, hydrolytic stability, seal compatibility and wear
protection.
[0005] Such oils are currently being formulated preferentially with PAO (especially PAO
6) or group I, II or Group III mineral oils as carrier fluids, and with specific polymers
like polyisobutylenes (PIBs), olefin copolymers (ethylene/propylene copolymers; OCPs),
polyalkyl methacrylates (PMAs) as thickeners or viscosity index improvers in addition
to the customary additive components.
[0006] Together with PAOs, low-viscosity esters are typically used in lubricant compositions,
for example esters like DIDA (diisodecyl adipate), DITA (diisotridecyl adipate) or
TMTC (trimethylolpropane caprylate), especially as solubilizers for polar additive
types. The common esters are available by known preparation methods, and preferably
from the reaction of an acid with an alcohol.
[0007] Although a wide variety of different carboxylic acid esters were developed for their
use in lubricants, there is still a need for novel carboxylic acid esters which have
an optimized viscosity profile over a broad temperature range, particularly at low
temperatures, as well as low pour points, high viscosity index, good hydrolytic and
oxidation stability high seal compatibility and favourable traction profile.
[0008] Over the previous decades environmental awareness has developed in many technical
fields including the field of lubricant compositions. Accordingly, base oils of natural
origin have found broad application in lubricant compositions thereby complementing
the usual synthetic or mineral oils and fluids.
[0009] It still appears to be difficult to completely eliminate synthetic components of
non-renewable origin in lubricating compositions due to the large industrial supply
of synthetic oils and similar fluids from the global fuel producing and fuel refining
industry, there is nonetheless growing interest in the industry to return to lubricating
components at least partially or even completely derived from renewable sources.
[0010] Accordingly, there is the additional objective to increase the carbon content of
renewable origin in lubricating compositions.
[0011] It is another object of the present invention to provide thermally and hydrolytically
stable esters that can be used for the preparation of lubricants with favourable viscosity
profiles over a broad temperature range including low temperatures.
[0012] The above objectives were met by preparing 2,5-furandicarboxylic acid esters obtained
by reacting a mixture of branched or linear, substituted or un-substituted aliphatic
C6 to C20 alcohols with 2,5-furandicarboxylic acid.
[0013] Thus, the present invention is directed to the use of a 2,5-furandicarboxylic acid
ester obtainable by reacting a mixture comprising
- a) 2,5-furandicarboxylic acid, and
- b) at least one alcohol of the general formula R-OH, wherein R represents a branched
or linear, substituted or unsubstituted, preferably un-substituted, aliphatic C6 to
C20 radical,
as a lubricant.
[0014] "Aliphatic C6 to C20 radical" means a saturated or unsaturated, preferably saturated,
nonaromatic hydrocarbon moiety having the specified number of carbon atoms (e.g. having
6 to 20 carbon atoms, i.e. 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, 18, 19 or 20
carbon atoms). In the sense of the presently claimed invention, "aliphatic C6 to C20
radicals" also include radicals wherein up to three, preferably 1 or 2, carbon atoms
in the straight- or branched-chain have been replaced with a heteroatom independently
selected from NH, O or S.
[0015] In connection with "aliphatic C6 to C20 radical", the term "substituted" within the
scope of this invention is to be understood as meaning the substitution of hydrogen
by 1, 2, 3, 4 or 5 substituents selected from the group consisting of F, Cl, Br, I,
CN, NH
2, NH-C
1-6-alkyl, NH-C
1-6-alkylene-OH, N(C
1-6-alkyl)
2, N(C
1-6-alkylene-OH)
2, NO
2, SH, S-C
1-6-alkyl, S-benzyl, O-C
1-6-alkyl, O-C
1-6-alkylene-OH, =O, O-benzyl, C(=O)C
1-6-alkyl, CO
2H, CO
2-C
1-6-alkyl, phenyl or benzyl. The substitution of hydrogen occurs either on different
atoms or on the same atom or at different positions. Polysubstitution can be carried
out with the same or with different substituents.
[0016] In another preferred embodiment of the present invention, the claimed use of the
2,5-furandicarboxylic acid ester is further characterized in that R is selected from
the group consisting of hexyl, heptyl, octyl, nonyl, decyl, undecyl, dodecyl, tridecyl,
tetradecyl, pentadecyl, hexadecyl, heptadecyl, octadecyl, 2-ethylhexyl, 2-propylheptyl,
2-butyloctyl, 2-pentylnonyl, 2-hexyldecyl, isohexyl, isoheptyl, isooctyl, isononyl,
isodecyl, isoundecyl, isododecyl, isotridecyl, isotetradecyl, isopentadecyl, isohexadecyl,
isoheptadecyl, isooctadecyl and mixtures thereof.
[0017] In another preferred embodiment of the present invention, the claimed use of the
2,5-furandicarboxylic acid ester is further characterized in that R is a mixture of
different radicals in which at least 65 mole percent of the radicals have the general
formula (I),

wherein p is 0, 1, 2, 3 or 4.
[0018] In another preferred embodiment of the present invention, the claimed use of the
2,5-furandicarboxylic acid ester is further characterized in that at least 80 mole
percent of the radicals R have the general formula (I),

wherein p is 0, 1, 2, 3 or 4.
[0019] In another preferred embodiment of the present invention, the claimed use of the
2,5-furandicarboxylic acid ester is further characterized in that p is 0, 1 or 2.
[0020] In another preferred embodiment of the present invention, the claimed use of the
2,5-furandicarboxylic acid ester is further characterized in that the 2,5-furanedicarboxylic
acid and/or the at least one alcohol of the general formula R-OH is at least partially
derived from a renewable source.
[0021] In another preferred embodiment of the present invention, the claimed use of the
2,5-furandicarboxylic acid ester is further characterized in that at least 40 mole
percent of the 2,5-furanedicarboxylic acid based on the total amount of 2,5-furanedicarboxylic
acid in the mixture are derived from a renewable source and/or at least 40 mole percent
of the at least one alcohol of the general formula R-OH based on the total amount
of the at least one alcohol of the general formula R-OH in the mixture are derived
from a renewable source.
[0022] The present invention is also directed to a lubricant composition comprising the
claimed 2,5-furandicarboxylic acid ester as defined above.
[0023] In another preferred embodiment of the present invention, the claimed lubricant composition
further includes a base oil component and an additive.
[0024] In another preferred embodiment of the present invention, the claimed lubricant composition
comprises the following components:
- 5.0 to 25.0 wt.-% of the 2,5-furandicarboxylic acid ester as defined above,
- 40.0 to 90.0 wt.-% of a base oil component,
- 0.1 to 20.0 wt.-% additives,
based on the total weight of the lubricant composition.
[0025] The present invention is also directed to a process for preparing the 2,5-furandicarboxylic
acid ester as defined above, comprising the steps of:
- providing 2,5-furandicarboxylic acid from a non-renewable source and/or a renewable
source,
- preparing a mixture of the 2,5-furandicarboxylic acid and at least one branched or
linear, substituted or un-substituted, preferably un-substituted, aliphatic C6 to
C20 alcohol of the general formula R-OH derived from a non-renewable source and/or
a renewable source,
- carrying out esterification of the 2,5-furandicarboxylic acid and the at least one
branched or linear, substituted or un-substituted aliphatic C6 to C20 alcohol of the
general formula R-OH.
[0026] In another preferred embodiment of the present invention, the claimed process for
preparing the 2,5-furandicarboxylic acid ester is further characterized in that R
is a mixture of different radicals in which at least 80 mole percent of the radicals
have the general formula (I),

wherein p is 0, 1, 2, 3 or 4.
[0027] In another preferred embodiment of the present invention, the claimed process for
preparing the 2,5-furandicarboxylic acid ester is further characterized in that at
least 40 mole percent of the 2,5-furandicarboxylic acid based on the total amount
of 2,5-furandicarboxylic acid used in the process and/or at least 40 mole percent
of the at least one alcohol of the general formula R-OH based on the total amount
of the the at least one alcohol of the general formula R-OH used in the process are
derived from a renewable source.
[0028] The present invention is further directed to the use of the lubricant composition
as defined above in an automatic transmission fluid, a manual transmission fluid,
a hydraulic fluid, a grease, a gear fluid, a metal-working fluid, a crankcase engine
oil or shock absorber fluid.
[0029] In another preferred embodiment of the present invention, the claimed process for
preparing the 2,5-furandicarboxylic acid ester is further characterized in that 100
mole percent of the 2,5-furandicarboxylic acid based on the total amount of 2,5-furandicarboxylic
acid used in the process and/or 100 mole percent of the at least one alcohol of the
general formula R-OH based on the total amount of the at least one alcohol of the
general formula R-OH used in the process are derived from a renewable source.
[0030] 2,5-Furandicarboxylic acid ((FDCA, CAS Nr. 3238-40-2) is commercially available or
can be prepared by processes known in the literature. Alternatively or additionally,
2,5-furandicarboxylic acid can be obtained from natural, preferably renewable, sources.
[0031] Processes for preparing 2,5-furanedicarboxylic acid can be found in Lewkowski
et al, "Synthesis, Chemistry and Application of 5- hydroxymethylfurfural and its derivatives"
(
Lewkowski et al., ARKIVOC 2001 (i), pages 17-54, ISSN 1424-6376). Most of these preparation methods are based on acid-catalyzed reaction of carbohydrates,
especially glucose, fructose, preferably fructose to 5-hydroxyfurfural (5-HMF), which
can be isolated from the reaction mixture by process technology like for instance
by the so-called two-phase operation mode. For instance, respective descriptions are
disclosed in
Leshkov et al., Science 2006, vol. 312, pages 1933-1937 and in
Zhang et al., Angewandte Chemie 2008, vol. 120, pages 9485-9488. The obtained 5-HMF can then be further oxidized to 2,5-furandicarboxylic acid in
an additional process step, as for example disclosed by
Christensen in ChemSusChem 2007, vol. 1, pages 75-78.
[0032] Renewable sources for obtaining 2,5-furandicarboxylic acid preferably include various
vegetable sources, which are used for the production of fructose and glucose or similar
carbohydrates. Preferably fructose and/or glucose syrups and/or non-edible carbohydrates
such as (hemi)-cellulose-based carbohydrates can be used as starting materials.
[0033] The 2,5-furandicarboxylic acid to be used in the preparation of the 2,5-furandicarboxylic
acid ester which are used as lubricants in the present invention can be either of
pure synthetic (preferably non-renewable) origin or of renewable origin. Preferably,
the 2,5-furandicarboxylic acid is a mixture of synthetic material together with material
that is at least partially derived from a renewable source. Most preferred is 2,5-furandicarboxylic
acid of (fully) renewable origin.
[0034] 2,5-Furandicarboxylic acid of synthetic, non-renewable origin refers to 2,5-furandicarboxylic
acid that has been prepared by chemical technology starting from a material and/or
compound which is not of renewable origin.
[0035] 2,5-Furandicarboxylic acid of renewable origin refers to 2,5-furandicarboxylic acid
that has been obtained from material and/or a compound obtained from a vegetable source,
preferably from agricultural production of a certain plant in which 2,5-furandicarboxylic
acid is directly formed during the normal growth cycle of this plant and/or in which
the normal growth cycle of said plant leads to the formation of a plant product, like
preferably glucose and/or fructose or further products derived therefrom like glucose
syrup, that can be subsequently processed by chemical technology or biotechnological
transformation into 2,5-furandicarboxylic acid.
[0036] The plant in which the 2,5-furandicarboxylic acid or the material to be processed
into 2,5-furandicarboxylic acid is formed can be a genetically modified (genetically
engineered by recombinant DNA or RNA technology) plant. Alternatively or additionally,
the 2,5-furandicarboxylic acid is obtained starting from material obtained from a
natural, wild-type plant which has not been modified by recombinant technology.
[0037] When providing the 2,5-furandicarboxylic acid for obtaining the 2,5-furandicarboxylic
acid ester used as lubricant in the present invention, at least 40 mole percent of
the 2,5-furandicarboxylic acid based on the total amount of 2,5-furandicarboxylic
acid used in the preparation of the 2,5-furandicarboxylic acid ester are preferably
derived from a renewable source or origin. More preferably, at least 50 mole percent,
or more preferably at least 65 mole percent, even more preferably at least 75 mole
percent, and most preferably at least 85 mole percent of the 2,5-furandicarboxylic
acid used for obtaining the 2,5-furandicarboxylic acid ester to be used as lubricant
in the present invention can be derived from a renewable source in the claimed preparation
process.
[0038] However, in another very preferred embodiment of the present invention, the 2,5-furandicarboxylic
acid ester to be used as lubricant in the present invention is obtained from 2,5-furandicarboxylic
acid which is fully of renewable origin, i.e. the 2,5-furandicarboxylic acid consists
of at least 90 mole percent, at least 95 mole percent, or even 100 mole percent of
material from a renewable source.
[0039] Regarding the grade of chemical purity, 2,5-furandicarboxylic acid as used in the
present invention is either substantially pure, i.e. includes at least 80 percent
by weight, preferably at least 90 percent by weight, more preferably at least 95 percent
by weight, even more preferably at least 97 percent by weight, even more preferably
at least 98.0 percent by weight, or most preferably at least 99.0 percent by weight,
or even at least 99.5 percent by weight of 2,5-furandicarboxylic acid, based on the
total amount of the corresponding sample of 2,5-furandicarboxylic acid.
[0040] In addition, 2,5-furandicarboxylic acid as used in the present invention preferably
has very low level of unsaturated components. The content of unsaturated components
is normally less than 5 percent by weight, preferably less than 3 percent by weight,
more preferably less than 1 percent by weight, even more preferably less than 0.5
percent by weight, and most preferably less than 0.1 percent by weight, based on the
total weight of 2,5-furandicarboxylic acid.
[0041] Most generically, the at least one alcohol of the general formula R-OH to be used
in the preparation of the 2,5-furandicarboxylic acid ester to be used as lubricant
in the present invention is defined by a radical R representing a branched or linear,
substituted or unsubstituted aliphatic hydrocarbon moiety having from 6 to 20 carbon
atoms.
[0042] Most preferably, the radical R denotes a moiety selected from the group consisting
of hexyl, heptyl, octyl, nonyl, decyl, undecyl, dodecyl, tridecyl, tetradecyl, pentadecyl,
hexadecyl, heptadecyl, octadecyl, 2-ethylhexyl, 2-propylheptyl, 2-butyloctyl, 2-pentylnonyl,
2-hexyldecyl, isohexyl, isoheptyl, isooctyl, isononyl, isodecyl, isoundecyl, isododecyl,
isotridecyl, isotetradecyl, isopentadecyl, isohexadecyl, isoheptadecyl, isooctadecyl
and mixtures thereof.
[0043] Even more preferably, the radical R denotes a branched or linear, substituted or
unsubstituted aliphatic hydrocarbon moiety having from 8 to 18 carbon atoms, or even
more preferably, 8 to 16 carbon atoms.
[0044] Especially preferred moieties having 8 to 18 carbon atoms include octyl, nonyl, decyl,
undecyl, dodecyl, tridecyl, tetradecyl, pentadecyl, hexadecyl, heptadecyl, octadecyl,
2-ethylhexyl, 2-propylheptyl, 2-butyloctyl, 2-pentylnonyl, 2-hexyldecyl, isohexyl,
isoheptyl, isooctyl, isononyl, isodecyl, isoundecyl, isododecyl, isotridecyl, isotetradecyl,
isopentadecyl, isohexadecyl, isoheptadecyl, isooctadecyl and mixtures thereof.
[0045] Especially preferred moieties having 8 to 16 carbon atoms include octyl, nonyl, decyl,
undecyl, dodecyl, tridecyl, tetradecyl, pentadecyl, hexadecyl, 2-ethylhexyl, 2-propylheptyl,
2-butyloctyl, 2-pentylnonyl, 2-hexyldecyl, isohexyl, isoheptyl, isooctyl, isononyl,
isodecyl, isoundecyl, isododecyl, isotridecyl, isotetradecyl, isopentadecyl, isohexadecyl,
and mixtures thereof.
[0046] The alcohol with the radical R being 2-propylheptyl, i.e. 2-propylheptanol, is commercially
available from BASF SE, Ludwigshafen and represents a mixture of 93.0 wt.-% 2-propyl-heptanol,
2.9 wt.-% 2-propyl-4-methyl-hexanol, 3.9 wt.-% 2-propyl-5-methylhexanol and 0.2 wt.-%
2-isopropylheptanol.
[0047] When providing the at least one branched or linear, substituted or unsubstituted
aliphatic C6 to C20 alcohol for obtaining the 2,5-furandicarboxylic acid ester to
be used as lubricant in the present invention, at least 40 mole percent of the at
least one alcohol of the general formula R-OH based on the total amount of theat least
one alcohol of the general formula R-OH used in the preparation of the 2,5-furandicarboxylic
acid ester are preferably derived from a renewable source or origin. Preferably, at
least 50 mole percent, more preferably at least 65 mole percent, even more preferably
at least 75 mole percent, and most preferably at least 85 mole percent of the at least
one alcohol of the general formula R-OH used for obtaining the 2,5-furandicarboxylic
acid ester to be used as lubricant in the present invention can be derived from a
renewable source in the claimed preparation process. The term at least one branched
or linear, substituted or unsubstituted aliphatic C6 to C20 alcohol "of renewable
origin" is defined in a similar manner like 2,5-furandicarboxylic acid of renewable
origin is defined above. Accordingly, an alcohol of renewable origin is one which
is prepared, isolated or derived starting from a natural, renewable source or material
obtained for instance from a plant.
[0048] In one preferred embodiment of the present invention, the 2,5-furandicarboxylic acid
ester is obtained from 2,5-furandicarboxylic acid of renewable origin, exclusively,
and the at least one branched or linear, substituted or unsubstituted aliphatic C6
to C20 alcohol, especially a mixture of Guerbet alcohols as defined herein, which
also is of renewable origin, exclusively. Accordingly, it is preferred that the 2,5-furandicarboxylic
acid ester is formed exclusively from components of renewable origin.
[0049] Alternatively, the 2,5-furandicarboxylic acid and/or the at least one branched or
linear, substituted or unsubstituted aliphatic C6 to C20 alcohol are only partially
derived from a renewable source thereby leading to a 2,5-furandicarboxylic acid ester
which is also only of partial renewable origin based on the combined amounts of the
respective partial amount of 2,5-furandicarboxylic acid of renewable origin and the
respective partial amount of the at least one branched or linear, substituted or unsubstituted
aliphatic C6 to C20 alcohol, especially a mixture of Guerbet alcohols as defined herein,
of renewable origin.
[0050] One preferred alcohol of the general formula R-OH, or mixture of alcohols R-OH, which
is used in the present invention for preparing the 2,5-furandicarboxylic acid ester
to be used as lubricant in the present invention, is a so-called "Guerbet alcohol".
[0052] The term "Guerbet alcohol" as used in the present invention relates to alcohols,
or a mixture of alcohols, which is obtained by the so-called Guerbet reaction. Accordingly,
the mixture of alcohols as used in the present invention for obtaining the 2,5-furandicarboxylic
acid ester to be used as lubricant in the present invention is a mixture of alcohols
obtained from the Guerbet reaction, particularly as defined in the above references.
[0053] In the course of the Guerbet reaction, primary alcohols are ultimately dimerized
to α-branched primary alcohols in the presence of suitable catalysts. According to
the literature, the primary products formed from the alcohols are aldehydes which
subsequently dimerize to saturated alcohols by aldol condensation with elimination
of water and subsequent hydrogenation. As well as the main product, different by-products
can also form, for example unsaturated α-branched primary alcohols if the hydrogenation
of the double bond does not proceed to completion, or more particularly α-branched
primary alcohols which have additional branches in the side chain or main chain.
[0054] In another embodiment, one preferred R radical of the at least one branched or linear,
substituted or unsubstituted aliphatic alcohol of the general formula R-OH is a radical
derived from a Guerbet alcohol, i.e. obtained from the Guerbet reaction comprising
or containing a mixture of different radicals in which at least 50 mole %, or 65 mole
percent, more preferably at least 70 mole percent, even more preferably at least 80
mole %, and most preferably at least 90 mole % of the radicals based on the total
amount of radicals in the mixture have the general formula (I),

wherein p is 0, 1, 2, 3 or 4; preferably 0,1 or 2, and more preferably 2;
[0055] The invention further relates to the use of the claimed 2,5-furandicarboxylic acid
esters as additives, co-solvents or base oils in lubricant compositions and fuel additives.
[0056] By the terms "lubricant" or "lubricant composition", as used in the presently claimed
invention, is meant a substance or composition capable of reducing friction between
moving surfaces.
[0057] The lubricant compositions according to the present invention can comprise the 2,5-furandicarboxylic
acid esters as one important component, for instance in a rather limited amount of
from 0.1 to 50.0 percent by weight, preferably 3.0 to 40.0 percent by weight, more
preferably 5.0 to 30.0 percent by weight, or even more preferably 10.0 to 25.0 percent
by weight, or, alternatively, as main component in the lubricant composition of the
present invention, in an amount of from 50.0 percent by weight to 100.0 percent by
weight, preferably 60.0 percent by weight to 95.0 percent by weight, more preferably
65.0 percent by weight to 90.0 percent by weight, or even more preferably 75.0 percent
by weight to 85.0 percent by weight, based on the total amount of lubricant composition.
[0058] In another preferred embodiment of the present invention, the 2,5-furandicarboxylic
acid esters are preferably used in an amount of 3.5 to 45 percent by weight, more
preferably in an amount of from 5.0 to 35.0 percent by weight, and most preferably
in an amount of 10.0 to 30.0 percent by weight, based on the total amount of the lubricant
composition.
[0059] One preferred lubricant composition of the present invention includes the following
components:
- 5.0 to 25.0 wt.-% of 2,5-furandicarboxylic acid ester as defined above,
- 40.0 to 90.0 wt.-% of a base oil component,
- 0.1 to 20.0 wt.-% additives,
based on the total weight of the lubricant composition, wherein, preferably, the additives
can include viscosity index improvers, like PMAs, OCPs and/or PIBs, in an amount of
10 to 30 wt.-%.
[0060] The following further lubricant compositions comprising the 2,5-furandicarboxylic
acid ester to be used as lubricant in the present invention are also preferred (all
numbers in percent by weight); the second range given ("or") is an even more preferred
range, respectively:
|
Lubricant type A |
Lubricant type B |
Lubricant type C |
Base oil |
50.0 to 85.0; or 65.0 to 75.0; |
25.0 to 75.0; or 35.0 to 65.0; |
0 to 45.0; or 5.0 to 20.0; |
2,5-furandicarboxylic acid ester |
5.0 to 20.0; or 10.0 to 17.0; |
20.0 to 50.0; or 30.0 to 45.0; |
50.0 to 85.0; or 60.0 to 80.0; |
Additives |
10.0 to 30.0; or 15.0 to 25.0; |
5.0 to 25.0; or 10.0 to 20.0; |
5.0 to 15.0; or 8.0 to 13.0; |
[0061] The following lubricant compositions are especially preferred (all numbers in percent
by weight); the second range ("or") given is an even more preferred range, respectively:
|
Lubricant type A' |
Lubricant type B' |
Lubricant type C' |
Base oil |
40.0 to 78.0; or 45.0 to 70.0; |
25.0 to 75.0; or 32.0 to 60.0; |
0 to 45.0; or 20.0 to 30.0; |
2,5-furandicarboxylic acid ester |
5.0 to 15.0; or 8.0 to 15.0; |
20.0 to 50.0; or 30.0 to 40.0; |
50.0 to 85.0; or 65.0 to 80.0; |
Additives (without VI improvers) |
5.0 to 15.0; or 8.0 to 15.0; |
0 to 10.0; or 5.0 to 8.0; |
0.0 to 5.0; or 2.0 to 4.0; |
Additives (VI improvers only) |
5.0 to 30.0; or 10.0 to 28.0; |
5.0 to 15.0; or 8.0 to 12.0; |
5.0 to 10.0; or 6.0 to 8.0; |
[0062] Viscosity index (VI) improvers are one possible class of additives that can be optionally
used in the lubricant compositions of the present invention. Examples of viscosity
index improvers include for instance OCPs, PMAs and/or PIBs, and are also disclosed
below where the additives are listed in more detail (see point 5).
[0063] The lubricant compositions according to the present invention may further include
base oils or co-solvents.
[0064] Preferred base oils contemplated for optional use in the lubricating oil compositions
according to the present invention include mineral oils, poly-alpha-olefin synthetic
oils and mixtures thereof.
[0065] Suitable base oils also include base stocks obtained by isomerization of synthetic
wax and slack wax, as well as base stocks produced by hydrocracking (rather than solvent
extracting) the aromatic and polar components of the crude. In general, both the mineral
and synthetic base oils will each have a kinematic viscosity ranging from about 1
to about 40 cSt at 100°C, although typical applications will require each oil to have
a viscosity ranging from about 1 to about 10 cSt at 100°C.
[0066] The mineral oils useful as optional components in the lubricant compositions according
to the present invention include all common mineral oil base stocks. This includes
oils that are naphthenic, paraffinic or aromatic in chemical structure.
[0067] Naphthenic oils are made up of methylene groups arranged in ring formation with paraffinic
side chains attached to the rings. The pour point is generally lower than the pour
point for paraffinic oils.
[0068] Paraffinic oils comprise saturated, straight chain or branched hydrocarbons.
[0069] The straight chain paraffins of high molecular weight raise the pour point of oils
and are often removed by dewaxing.
[0070] Aromatic oils are hydrocarbons of closed carbon rings of a semi-unsaturated character
and may have attached side chains. This oil is more easily degraded than paraffinic
and naphthalenic oils leading to corrosive by-products.
[0072] Further optional base oils include gas to liquid oils (GTL). Gaseous sources include
a wide variety of materials such as natural gas, methane, C1-C3 alkanes, landfill
gases, and the like. Such gases may be converted to liquid hydrocarbon products suitable
for use as lubricant base oils by a gas to liquid (GTL) process, such as the process
described in
U.S. patent 6,497,812, of which the disclosure is incorporated herein by reference.
[0073] Base oils derived from a gaseous source, hereinafter referred to as "GTL base oils",
typically have a viscosity index of greater than about 130, a sulfur content of less
than about 0.3 percent by weight, contain greater than about 90 percent by weight
saturated hydrocarbons (isoparaffins), typically from about 95 to about 100 percent
by weight branched aliphatic hydrocarbons, have a pour point of below -15 to -20°C.
[0074] The GTL base oils may be mixed with more conventional base oils such as Groups I
to V as specified by API. For example, the base oil component of the lubricant compositions
of the present invention may include 1 to 100 percent by weight of GTL base oil.
[0075] Thus, the lubricating oil composition of the present invention may optionally be
at least partially derived from a gaseous source.
[0076] Oils may be refined by conventional methodology using acid, alkali, and clay or other
agents such as aluminum chloride, or they may be extracted oils produced, for example,
by solvent extraction with solvents such as phenol, sulfur dioxide, furfural, dichlordiethyl
ether, etc.
[0077] They may be hydro-treated or hydro-refined, dewaxed by chilling or catalytic dewaxing
processes, or hydro-cracked. The mineral oil may be produced from natural crude sources
or be composed of isomerized wax materials or residues of other refining processes.
The preferred synthetic oils are oligomers of a-olefins, particularly oligomers of
1-decene, also known as polyalphaolefins or PAO's.
[0078] The base oils may be derived from refined, re-refined oils, or mixtures thereof.
Unrefined oils are obtained directly from a natural source or synthetic source (e.g.,
coal, shale, or tar sands bitumen) without further purification or treatment. Examples
of unrefined oils include a shale oil obtained directly from a retorting operation,
petroleum oil obtained directly from distillation, or ester oil obtained directly
from an esterification process, each of which is then used without further treatment.
Refined oils are similar to the unrefined oils except that refined oils have been
treated in one or more purification steps to improve one or more properties. Suitable
purification techniques include distillation, hydro-treating, dewaxing, solvent extraction,
acid or base extraction, filtration, and percolation, all of which are known to those
skilled in the art. Re-refined oils are obtained by treating used oils in processes
similar to those used to obtain the refined oils. These re-refined oils are also known
as reclaimed or reprocessed oils and are often additionally processed by techniques
for removal of spent additives and oils breakdown products.
[0079] In the lubricant compositions according to the present invention comprising the 2,5-furandicarboxylic
acid ester of the present invention, it is optional to include other esters being
capable of reducing friction between moving surfaces.
[0080] For instance, the lubricant compositions of the present invention can further comprise
other monocarboxylic acid esters or dicarboxylic acid esters. Both additional types
of optional esters are suitable for reducing friction and can be added together or
individually to the lubricant compositions of the present invention.
[0081] The monocarboxylic and dicarboxylic acid esters that can be optionally used in addition
are present in the lubricant compositions either individually, or in the form of mixtures
comprising at least one monocarboxylic acid ester and at least one dicarboxylic acid
ester.
[0082] Such monocarboxylic and dicarboxylic acid esters are obtained from known procedures,
preferably by esterification of the corresponding monocarboxylic and/or dicarboxylic
acid with the corresponding alcohol or mixture of alcohols.
[0083] Representative monocarboxylic acids include n-butanoic acid, n-pentanoic acid, n-hexanoic
acid, n-heptanoic acid, n-octanoic acid, n-nonanoic acid, n-decanoic acid, isobutanoic
acid, isopentanoic acid, isohexanoic acid, isoheptanoic acid, isooctanoic acid, 2-ethylhexanoic
acid, isononanoic acid, 3,5,5-trimethylhexanoic acid, and isodecanoic acid.
[0084] Representative dicarboxylic acid esters can be obtained from aliphatic dicarboxylic
acids. In preferred modes of the present invention, the optional dicarboxylic acid
esters can be obtained from dicarboxylic acids selected from the group consisting
of glutaric acid, diglycolic acid, succinic acid, azelaic acid, sebacic acid, 1,4-cyclohexanedicarboxylic
acid, adipic acid, 2,6-decahydronaphthalene dicarboxylic acid, 1,3-cyclohexanedicarboxylic
acid, and 2,5-norbornanedicarboxylic acid. A very preferred aliphatic dicarboxylic
acid is adipic acid. Instead of the acids, their anhydrides can also be used.
[0085] Representative alcohols to be used for obtaining other optional monocarboxylic acid
esters and/or dicarboxylic acid esters include 2-propylheptanol, 2-propyl-4-methyl-hexanol,
2-propyl-5-methyl-hexanol, 2-isopropyl-4-methyl-hexanol, 2-isopropyl-5-methyl-hexanol,
2-propyl-4,4-dimethylpentanol, 2-ethyl-2,4-dimethylhexanol, 2-ethyl-2-methyl-heptanol,
2-ethyl-2,5-dimethylhexanol and 2-isopropyl-heptanol.
[0086] Preferably the alcohol mixture comprises 80 to 95 percent by weight of 2-n-propyl-heptanol,
1.0 to 10 percent by weight of 2-propyl-4-methyl-hexanol, 1.0 to 10 percent by weight
of 2-propyl-5-methyl-hexanol and 0.1 to 2.0 percent by weight of 2-isopropyl-heptanol,
whereby the weight of each component is related to the total weight of the monoalcohols.
[0087] More preferably the mixture comprises 91.0 to 95.0 percent by weight of 2-n-propyl-heptanol,
2.0 to 5.0 percent by weight of 2-propyl-4-methyl-hexanol, 3.0 to 5.0 percent by weight
of 2-propyl-5-methyl-hexanol and 0.1 to 0.8 percent by weight of 2-isopropyl-heptanol,
whereby the weight of each component is related to the total weight of the monoalcohols.
[0088] In another embodiment, an additional optional carboxylic acid ester is obtained by
reacting a mixture comprising adipic acid, 2-propyl-heptanol, 2-propyl-4-methyl-hexanol
and 2-propyl-5-methyl-hexanol.
[0089] In another embodiment, an additional optional carboxylic acid ester to be present
in the lubricant compositions of the present invention is obtained by reacting a mixture
comprising adipic acid and 80 to 95 percent by weight of 2-n-propyl-heptanol, 1.0
to 10 percent by weight of 2-propyl-4-methyl-hexanol, 1.0 to 10 percent by weight
of 2-propyl-5-methyl-hexanol, and 0.1 to 2.0 percent by weight of 2-isopropyl-heptanol,
whereby the weight of each component is related to the total weight of the monoalcohols.
[0090] The addition of at least one additive, like an additional customary oil additive,
to the lubricating oil compositions of the present invention is possible but not mandatory
in every case. The mentioned lubricant compositions, e.g. greases, gear fluids, metal-working
fluids and hydraulic fluids, may additionally comprise further additives that are
added in order to improve their basic properties still further.
[0091] Such additives include: further antioxidants or oxidation inhibitors, corrosion inhibitors,
friction modifiers, metal passivators, rust inhibitors, anti-foamants, viscosity index
enhancers, additional pour-point depressants, dispersants, detergents, further extreme-pressure
agents and/or anti-wear agents.
[0092] Such additives are present in the amounts customary for each of them, which range
in each case from 0.01 to 30.0 percent by weight, preferably from 0.05 to 20.0 percent
by weight, more preferably from 0.1 to 10.0 percent by weight, and even more preferably
0.2 to 5.0 percent by weight, based on the total weight of the lubricating oil composition.
Examples of further additives are given below:
- 1. Examples of phenolic antioxidants:
1.1. Alkylated monophenols: 2,6-di-tert-butyl-4-methylphenol, 2-butyl-4,6-dimethylphenol,
2,6-di-tert-butyl-4-ethylphenol, 2,6-di-tert-butyl-4-n-butylphenol, 2,6-di-tert-butyl-4-isobutylphenol,
2,6-dicyclopentyl-4-methylphenol, 2-(alpha-methylcyclohexyl)-4,6-dimethylphenol, 2,6-dioctadecyl-4-methylphenol,
2,4,6-tricyclohexylphenol, 2,6-di-tert-butyl-4-methoxymethylphenol, linear nonylphenols
or nonylphenols branched in the side chain, such as, for example, 2,6-dinonyl-4-methylphenol,
2,4-dimethyl-6-(1'-methyl-undec-1'-yl)-phenol, 2,4-dimethyl-6-(1'-methylheptadec-1'-yl)-phenol,
2,4-dimethyl-6-(1'-methyltridec-1'-yl)-phenol and mixtures thereof;
1.2. Alkylthiomethylphenols: 2,4-dioctylthiomethyl-6-tert-butylphenol, 2,4-dioctylthiomethyl-6-methylphenol,
2,4-dioctylthiomethyl-6-ethylphenol, 2,6-didodecylthiomethyl-4-nonylphenol;
1.3. Hydroquinones and alkylated hydroquinones: 2,6-di-tert-butyl-4-methoxyphenol,
2,5-di-tert-butylhydroquinone, 2,5-di-tert-amylhydroquinone, 2,6-diphenyl-4-octadecyloxyphenol,
2,6-di-tert-butylhydroquinone, 2,5-di-tert-butyl-4-hydroxyanisole, 3,5-di-tert-butyl-4-hydroxyanisole,
3,5-di-tert-butyl-4-hydroxyphenyl stearate, bis(3,5-di-tert-butyl-4-hydroxyphenyl)
adipate;
1.4. Tocopherols: alpha-, beta-, gamma- or delta-tocopherol and mixtures thereof (vitamin
E);
1.5. Hydroxylated thiodiphenyl ethers: 2,2'-thio-bis(6-tert-butyl-4-methylphenol),
2,2'-thio-bis(4-octylphenol), 4,4'-thio-bis(6-tert-butyl-3-methylphenol), 4,4'-thio-bis(6-tert-butyl-2-methylphenol),
4,4'-thio-bis(3,6-di-sec-amylphenol), 4,4'-bis(2,6-dimethyl-4-hydroxy-phenyl)disulfide;
1.6. Alkylidene bisphenols: 2,2'-methylene-bis(6-tert-butyl-4-methylphenol), 2,2'-methylene-bis(6-tert-butyl-4-ethylphenol),
2,2'-methylene-bis[4-methyl-6-(alpha -methylcyclohexyl)phenol], 2,2'-methylene-bis(4-methyl-6-cyclohexylphenol),
2,2'-methylene-bis(6-nonyl-4-methylphenol), 2,2'-methylene-bis(4,6-di-tert-butylphenol),
2,2'-ethylidene-bis(4,6-di-tert-butylphenol), 2,2'-ethylidene-bis(6-tert-butyl-4-isobutylphenol),
2,2'-methylene-bis[6-(alpha -methylbenzyl)-4-nonylphenol], 2,2'-methylene-bis[6-(alpha,
alpha -dimethyl-benzyl)-4-nonylphenol], 4,4'-methylene-bis(2,6-di-tert-butylphenol),
4,4'-methylene-bis(6-tert-butyl-2-methylphenol), 1,1-bis(5-tert-butyl-4-hydroxy-2-methylphenyl)butane,
2,6-bis(3-tert-butyl-5-methyl-2-hydroxybenzyl)-4-methylphenol, 1,1,3-tris(5-tert-butyl-4-hydroxy-2-methylphenyl)butane,
1,1-bis(5-tert-butyl-4-hydroxy-2-methylphenyl)-3-n-dodecylmercaptobutane, ethylene
glycol bis[3,3-bis(3'-tert-butyl-4'-hydroxyphenyl)-butyrate], bis(3-tert-butyl-4-hydroxy-5-methylphenyl)dicyclopentadiene,
bis[2-(3'-tert-butyl-2'-hydroxy-5'-methylbenzyl)-6-tert-butyl-4-methylphenyl]terephthalate,
1,1-bis(3,5-dimethyl-2-hydroxyphenyl)butane, 2,2-bis(3,5-di-tert-butyl-4-hydroxyphenyl)-propane,
2,2-bis(5-tert-butyl-4-hydroxy-2-methylphenyl)-4-n-dodecylmercaptobutane, 1,1,5,5-tetra(5-tert-butyl-4-hydroxy-2-methylphenyl)pentane;
1.7. O-. N- and S-benzyl compounds: 3,5,3',5'-tetra-tert-butyl-4,4'-dihydroxydibenzyl
ether, octadecyl-4-hydroxy-3,5-dimethylbenzyl-mercaptoacetate, tridecyl-4-hydroxy-3,5-di-tert-butylbenzyl-mercaptoacetate,
tris(3,5-di-tert-butyl-4-hydroxybenzyl)amine, bis(4-tert-butyl-3-hydroxy-2,6-dimethylbenzyl)dithioterephthalate,
bis(3,5-di-tert-butyl-4-hydroxybenzyl)sulfide, isooctyl-3,5-di-tert-butyl-4-hydroxybenzyl-mercaptoacetate;
1.8. Hydroxybenzylated malonates: dioctadecyl-2,2-bis(3,5-di-tert-butyl-2-hydroxybenzyl)malonate,
dioctadecyl-2-(3-tert-butyl-4-hydroxy-5-methylbenzyl)malonate, didodecyl-mercaptoethyl-2,2-bis(3,5-di-tert-butyl-4-hydroxybenzyl)
malonate, di[4-(1,1,3,3-tetramethylbutyl)-phenyl]-2,2-bis(3,5-di-tert-butyl-4-hydroxybenzyl)malonate;
1.9. Hydroxybenzyl aromatic compounds: 1,3,5-tris(3,5-di-tert-butyl-4-hydroxybenzyl)-2,4,6-trimethylbenzene,
1,4-bis(3,5-di-tert-butyl-4-hydroxybenzyl)-2,3,5,6-tetramethylbenzene, 2,4,6-tris(3,5-di-tert-butyl-4-hydroxybenzyl)phenol;
1.10. Triazine compounds: 2,4-bis-octylmercapto-6-(3,5-di-tert-butyl-4-hydroxyanilino)-1,3,5-triazin
e, 2-octylmercapto-4,6-bis(3,5-di-tert-butyl-4-hydroxyanilino)-1,3,5-triazine, 2-octylmercapto-4,6-bis(3,5-di-tert-butyl-4-hydroxyphenoxy)-1,3,5-triazine,
2,4,6-tris(3,5-di-tert-butyl-4-hydroxyphenoxy)-1,2,3-triazine, 1,3,5-tris (3,5-di-tert-butyl-4-hydroxybenzyl)isocyanurate,
1,3,5-tris(4-tert-butyl-3-hydroxy-2,6-dimethylbenzyl)isocyanurate, 2,4,6-tris(3,5-di-tert-butyl-4-hydroxyphenylethyl)-1,3,5-triazine,
1,3,5-tris(3,5-di-tert-butyl-4-hydroxyphenylpropionyl)hexahydro-1,3,5-triazine, 1,3,5-tris(3,5-dicyclohexyl-4-hydroxybenzyl)isocyanurate;
1.11. Acylaminophenols: 4-hydroxylauric acid anilide, 4-hydroxystearic acid anilide,
N-(3,5-di-tert-butyl-4-hydroxyphenyl)-carbamic acid octyl ester;
1.12. Esters of beta-(5-tert-butyl-4-hydroxy-3-methylphenyl) propionic acid: with
polyhydric alcohols, e.g. with 1,6-hexanediol, 1,9-nonanediol, ethylene glycol, 1,2-propanediol,
neopentyl glycol, thiodiethylene glycol, diethylene glycol, triethylene glycol, pentaerythritol,
tris(hydroxyethyl)isocyanurate, N,N'-bis(hydroxyethyl) oxalic acid diamide, 3-thiaundecanol,
3-thiapentadecanol, trimethylhexanediol, trimethylolpropane, 4-hydroxymethyl-1-phospha-2,6,7-trioxabicyclo[2.2.2]octane;
1.13. Esters of beta-(3,5-di-tert-butyl-4-hydroxyphenyl) propionic acid, gamma-(3,5-dicyclohexyl-4-hydroxyphenyl)
propionic acid, 3,5-di-tert-butyl-4-hydroxyphenylacetic acid: with mono- or polyhydric
alcohols, e.g. with methanol, ethanol, n-octanol, isooctanol, octadecanol, 1,6-hexanediol,
1,9-nonanediol, ethylene glycol, 1,2-propanediol, neopentyl glycol, thiodiethylene
glycol, diethylene glycol, triethylene glycol, pentaerythritol, tris(hydroxyethyl)isocyanurate,
N,N'-bis-hydroxyethyl oxalic acid diamide, 3-thiaundecanol, 3-thiapentadecanol, trimethylhexanediol,
trimethylolpropane, 4-hydroxymethyl-1-phospha-2,6,7-trioxabicyclo[2.2.2]octane;
1.14. Amides of beta-(3,5-di-tert-butyl-4-hydroxyphenyl) propionic acid: N,N'-bis(3,5-di-tert-butyl-4-hydroxyphenylpropionyl)hexamethylenediamine,
N,N'-bis(3,5-di-tert-butyl-4-hydroxyphenylpropionyl)trimethylenediamine, N,N'-bis(3,5-di-tert-butyl-4-hydroxyphenylpropionyl)hydrazine;
1.15. Ascorbic acid (vitamin C);
1.16. Aminic antioxidants: N,N'-diisopropyl-p-phenylenediamine, N,N'-di-sec-butyl-p-phenylenediamine,
N,N'-bis(1,4-dimethylpentyl)-p-phenylenediamine, N,N'-bis(1-ethyl-3-methylpentyl)-p-phenylenediamine,
N,N'-bis(1-methylheptyl)-p-phenylenediamine, N,N'dicyclohexyl-p-phenylenediamine,
N,N'-diphenyl-p-phenylenediamine, N,N'-di(naphth-2-yl)-p-phenylenediamine, N-isopropyl-N'-phenyl-p-phenylenediamine,
N-(1,3-dimethylbutyl)-N'-phenyl-p-phenylenediamine, N-(1-methylheptyl)-N'-phenyl-p-phenylenediamine,
N-cyclohexyl-N'-phenyl-p-phenylenediamine, 4-(p-toluenesulfonamido)-diphenylamine,
N,N'-dimethyl-N,N'-di-sec-butyl-p-phenylenediamine, diphenylamine, N-allyldiphenylamine,
4-isopropoxydiphenylamine, 4-n-butylaminophenol, 4-butyrylaminophenol, 4-nonanoylaminophenol,
4-dodecanoylaminophenol, 4-octadecanoylaminophenol, di(4-methoxyphenyl)amine, 2,6-di-tert-butyl-4-dimethylaminomethyl
phenol, 2,4'-diaminodiphenylmethane, 4,4'-diaminodiphenylmethane, N,N,N',N'-tetramethyl-4,4'-diaminodiphenylmethane,
1,2-di[(2-methylphenyl)amino]-ethane, 1,2-di(phenylamino)propane, (o-tolyl)biguanide,
di[4-(1',3'-dimethylbutyl)phenyl]amine, tert-octylated N-phenyl-1-naphthylamine, mixture
of mono- and di-alkylated tert-butyl/tert-octyl-diphenylamines, mixture of mono- and
di-alkylated nonyidiphenylamines, mixture of mono- and di-alkylated dodecyldiphenylamines,
mixture of mono- and di-alkylated isopropyl/isohexyl-diphenylamines, mixtures of mono-
and di-alkylated tert-butyldiphenylamines, 2,3-dihydro-3,3-dimethyl-4H-1,4-benzothiazine,
phenothiazine, mixture of mono- and di-alkylated tert-butyl/tert-octylphenothiazines,
mixtures of mono- and di-alkylated tert-octylphenothiazines, N-allylphenothiazine,
N,N,N',N'-tetraphenyl-1,4-diaminobut-2-ene, N,N-bis(2,2,6,6-tetramethylpiperidin-4-yl)hexamethylenediamine,
bis(2,2,6,6-tetramethylpiperidin-4-yl)sebacate, 2,2,6,6-tetramethylpiperidin-4-one,
2,2,6,6-tetramethylpiperidin-4-ol.
- 2. Examples of further antioxidants: aliphatic or aromatic phosphites, esters of thiodipropionic
acid or thiodiacetic acid or salts of dithiocarbamic acid, 2,2,12,12-tetramethyl-5,9-dihydroxy-3,7,11-trithiamidecane
and 2,2,15,15-tetramethyl-5,12-dihydroxy-3,7, 10,14-tetrathiahexadecane.
- 3. Examples of metal deactivators, e.g. for copper:
3.1. Benzotriazoles and derivatives thereof: 2-mercaptobenzotriazole, 2,5-dimercaptobenzotriazole,
4- or 5-alkylbenzotriazoles (e.g. tolutriazole) and derivatives thereof, 4,5,6,7-tetrahydrobenzotriazole,
5,5'-methylene-bis-benzotriazole; Mannich bases of benzotriazole or tolutriazole,
such as 1-[di(2-ethylhexyl)aminomethyl]tolutriazole and 1-[di(2-ethylhexyl)aminomethyl]benzotriazole;
alkoxyalkylbenzotriazoles, such as 1-(nonyloxy-methyl)benzotriazole, 1-(1-butoxyethyl)-benzotriazole
and 1-(1-cyclohexyloxybutyl)-tolutriazole;
3.2. 1,2,4-Triazoles and derivatives thereof: 3-alkyl-(or -aryl-) 1,2,4-triazoles,
Mannich bases of 1,2,4-triazoles, such as 1-[di(2-ethylhexyl)aminomethyl]-1,2,4-triazole;
alkoxyalkyl-1,2,4-triazoles, such as 1-(1-butoxyethyl)-1,2,4-triazole; acylated 3-amino-1,2,4-triazoles;
3.3. Imidazole derivatives: 4,4'-methylene-bis(2-undecyl-5-methyl) imidazole and bis[(N-methyl)imidazol-2-yl]carbinol-octyl
ether;
3.4. Sulfur-containing heterocyclic compounds: 2-mercaptobenzothiazole, 2,5-dimercapto-1,3,4-thiadiazole,
2,5-dimercaptobenzothiadiazole and derivatives thereof; 3,5-bis[di(2-ethylhexyl)aminomethyl]-1,3,4-thiadiazolin-2-one;
3.5. Amino compounds: salicylidene-propylenediamine, salicylaminoguanidine and salts
thereof.
- 4. Examples of rust inhibitors:
4.1. Organic acids, their esters, metal salts, amine salts and anhydrides: alkyl-
and alkenylsuccinic acids and their partial esters with alcohols, diols or hydroxycarboxylic
acids, partial amides of alkyl- and alkenyl-succinic acids, 4-nonylphenoxyacetic acid,
alkoxy- and alkoxyethoxycarboxylic acids, such as dodecyloxyacetic acid, dodecyloxy
(ethoxy)acetic acid and amine salts thereof, and also N-oleoyl-sarcosine, sorbitan
monooleate, lead naphthenate, alkenylsuccinic acid anhydrides, e.g. dodecenylsuccinic
acid anhydride, 2-(2-carboxyethyl)-1-dodecyl-3-methylglycerol and salts thereof, especially
sodium and triethanolamine salts thereof.
4.2. Nitrogen-containing compounds:
4.2.1. Tertiary aliphatic or cycloaliphatic amines and amine salts of organic and
inorganic acids, e.g. oil-soluble alkylammonium carboxylates, and 1-[N,N-bis(2-hydroxyethyl)amino]-3-(4-nonylphenoxy)propan-2-ol;
4.2.2. Heterocyclic compounds: substituted imidazolines and oxazolines, e.g. 2-heptadecenyl-1-(2-hydroxyethyl)-imidazoline;
4.2.3. Sulfur-containing compounds: barium dinonyinaphthalene sulfonates, calcium
petroleum sulfonates, alkylthio-substituted aliphatic carboxylic acids, esters of
aliphatic 2-sulfocarboxylic acids and salts thereof.
- 5. Examples of additional viscosity index enhancers: polyacrylates, polymethacrylates
(PMAs), nitrogen containing polymethylmethacrylates, vinylpyrrolidone/methacrylate
copolymers, polyvinylpyrrolidones, polybutenes, polyisobutylenes (PIBs), olefin copolymers
such as ethylenepropylene copolymers (OCPs), styrene-isoprene copolymers, hydrated
styrene-isoprene copolymers, styrene/acrylate copolymers and polyethers. Multifunctional
viscosity improvers, which also have dispersant and/or antioxidancy properties are
known and may optionally be used in addition to the products of this invention. Conventional
polyisobutylenes (PIBs), like Lubrazol® 8406), and/or oligomeric copolymers (OCPs),
like Lubrazol® 8407 are one preferred addition of additional viscosity index improvers
in the lubricant composition of the present invention comprising 2,5-furandicarboxylic
acid esters.
- 6. Examples of pour-point depressants: polymethacrylates, ethylene/vinyl acetate copolymers,
alkyl polystyrenes, fumarate copolymers, alkylated naphthalene derivatives.
- 7. Examples of dispersants/surfactants: polybutenylsuccinic acid amides or imides,
polybutenylphosphonic acid derivatives, basic magnesium, calcium and barium sulfonates
and phenolates.
- 8. Examples of extreme-pressure and anti-wear additives: sulfur- and halogen-containing
compounds, e.g. chlorinated paraffins, sulfurized olefins or vegetable oils (soybean
oil, rape oil), alkyl- or aryl-di- or -tri-sulfides, benzotriazoles or derivatives
thereof, such as bis(2-ethylhexyl)aminomethyl tolutriazoles, dithiocarbamates, such
as methylene-bis-dibutyldithiocarbamate, derivatives of 2-mercaptobenzothiazole, such
as 1-[N,N-bis(2-ethylhexyl)aminomethyl]-2-mercapto-1H-1,3-benzothiazole, derivatives
of 2,5-dimercapto-1,3,4-thiadiazole, such as 2,5-bis(tert-nonyidithio)-1,3,4-thiadiazole.
- 9. Examples of coefficient of friction reducers: lard oil, oleic acid, tallow, rape
oil, sulfurized fats, amides, amines. Further examples are given in EP-A-0 565 487.
- 10. Examples of special additives for use in water/oil metal-working fluids and hydraulic
fluids: Emulsifiers: petroleum sulfonates, amines, such as polyoxyethylated fatty
amines, non-ionic surface-active substances; buffers: such as alkanolamines; biocides:
triazines, thiazolinones, tris-nitromethane, morpholine, sodium pyridenethiol; processing
speed improvers: calcium and barium sulfonates.
[0093] Depending on the end use applications, small quantities of additives such as anti-misting
agents may be also optionally added in an amount ranging from 0.05 to 5.0% by vol.
in one embodiment, and less than 1 wt. %, in other embodiments.
[0094] For certain applications, a small amount of foam inhibitors in the prior art can
also be added to the composition in an amount ranging from 0.02 to 15.0 wt. %.
[0095] The compositions may further comprise oil soluble metal deactivators in an amount
of 0.01 to 0.5 vol. % (based on the final oil volume).
[0096] Esterification of the 2,5-furandicarboxylic acid can be carried out according to
established procedures which are known to the skilled person. Additional detailed
descriptions for carrying out the esterification reaction are disclosed in
US 6,310,235,
US 5,324,853,
DE-A 2612355 (Derwent Abstract No. DW 77-72638 Y) or
DE-A 1945359 (Derwent Abstract No. DW 73-27151 U). These documents and the corresponding descriptions
therein are herewith incorporated by reference.
[0097] In a preferred embodiment of the preparation process of the present invention, the
2,5-furandicarboxylic acid esters to be used as lubricants in the present invention
can be obtained by initially providing 2,5-furandicarboxylic acid and/or the at least
one branched or linear, substituted or unsubstituted aliphatic C6 to C20 alcohol from
a non-renewable and/or renewable source as defined above. It is especially preferred
that all components from which the ester is formed, i.e. acid and alcohol is of renewable
origin.
[0098] In a first step, the 2,5-furandicarboxylic acid or a suitable derivative thereof
is provided. Preferably, the 2,5-furandicarboxylic acid can be esterified with the
at least one branched or linear, substituted or unsubstituted aliphatic C6 to C20
alcohol of the general formula R-OH by use of the corresponding acyl halogenide, preferably
the acyl chloride or acyl bromide, or the respective anhydride of 2,5-furandicarboxylic
acid.
[0099] Then, in a next step, a mixture is prepared of the 2,5-furandicarboxylic acid with
the at least one C6 to C20 alcohol of the general formula R-OH, wherein the radical
R denotes a branched or linear, substituted or unsubstituted aliphatic hydrocarbon
moiety having from 6 to 20 carbon atoms.
[0100] More preferably, the radical R denotes a branched or linear, substituted or unsubstituted
aliphatic hydrocarbon moiety having from 10 to 18 carbon atoms.
[0101] Most preferably, the radical R denotes a moiety selected from the group consisting
of decyl, isodecyl, undecyl, dodecyl, tridecyl, tetradecyl, pentadecyl, hexadecyl,
heptadecyl, octadecyl, 2-propylheptyl, 2-butyloctyl, 2-pentylnonyl and 2-hexyldecyl,
as well as mixtures thereof.
[0102] In another preferred embodiment of the preparation process of the present invention,
the mixture of the at least one alcohol of the general formula R-OH is preferably
the mixture of so-called Guerbet alcohols obtainable from the Guerbet reaction, wherein
the preferred radical R is a mixture of different radicals in which at least 50 mole
% or 65 mole percent, more preferably at least 70 mole percent, even more preferably
at least 80 mole %, and most preferably at least 90 mole %, of the total amount of
radicals used in this preparation process, have the general formula I,

wherein p is 0, 1, 2, 3, or 4; while p is preferably 0,1 or 2, or more preferably
p is 2;.
[0103] In the subsequent process stage or step, the esterification of the 2,5-furandicarboxylic
acid is carried out with the mixture of the at least one branched or linear, substituted
or unsubstituted aliphatic C6 to C20 alcohol of the general formula R-OH as defined
above. This esterification reaction of the 2,5-furandicarboxylic acid preferably includes
the following optional or preferred process features.
[0104] Esterification is typically carried out at a temperature range from 50 to 250°C.
Preferably, the mixture obtained in the previous step(s) is heated to a temperature
in the range of 80°C to 160°C, followed by optionally adding a basic aqueous solution,
and optionally followed in a third step by removing the remaining alcohol.
[0105] Esterification catalysts can also be optionally used, for instance mineral acids
like sulfuric acid or phosphoric acid, organic sulfonic acids like methanesulfonic
acid and p-toluenesulfonic acid; amphoteric catalysts, e.g. titanium-, tin(IV) or
zirconium compounds like tetraalkoxytitanium compounds, e.g. tetrabutoxytitanium,
and tin(IV)oxide. Water formed in this reaction can be optionally removed by common
methods, e.g. by distillation.
[0106] The esterification catalyst will be preferably used in an effective amount, typically
in the range of from 0.05 to 10 wt%, more preferably 0.1 to 5.0 wt% based on the combined
amount of acid component (or anhydride) and the alcohol component.
[0107] In more preferred embodiments of the present invention, when the esterification catalyst
is selected from organic acids or mineral acids, the esterification is preferably
carried out at a temperature range from 50 to 160°C. If the esterification catalyst
is selected from amphoteric catalysts, the esterification is preferably carried out
at a temperature range from 100 to 250°C, more preferably from 150°C to 200°C.
[0108] In alternative embodiments of the esterification process of the present invention,
the procedures according to
WO 02/038531 A1 can be included, either completely or only partially by only selecting at least one
of the following steps.
[0109] WO 02/038531 A1 discloses processes for the preparation of esters, comprising
- a) heating until reflux in a reaction zone a mixture essentially comprising an acid
component or an anhydride thereof and the alcohol component in the presence of an
optional esterification catalyst,
- b) separating by rectification the alcohol and water-containing vapor into an alcohol-rich
and a water-rich fraction, respectively,
- c) returning the alcohol-rich fraction to the reaction zone and removing the water-rich
fraction from the process.
[0110] Preferably, the esterification of 2,5-furandicarboxylic acid is carried out in the
presence of the above-described alcohol component by use of an organic acid or a mineral
acid, particularly sulfuric acid. In a very preferred embodiment, the alcohol component
is used in at least two-fold stochiometric amount relative to the 2,5-furandicarboxylic
acid or the derivative thereof, based on the reactive OH- and CO
2H-groups respectively. Other optional stochiometric ratios of reactive OH-groups to
CO
2H-groups include 1.0 to 4.0, preferably 1.2 to 3.5, even more preferably 1.4 to 3.0,
or 1.6 to 2.5.
[0111] The esterification of the present invention can be preferably carried out at ambient
pressure or decreased or increased pressure. Preferably, the esterification is carried
out at ambient pressure or decreased pressure.
[0112] The esterification of the present invention can be carried out in the absence of
an additional solvent or in the presence of an organic solvent, preferably an organic
solvent which is chemically inert under the esterification conditions. Examples for
organic solvents include aliphatic hydrocarbons, halogenated aliphatic hydrocarbons,
aromatic and substituted aromatic hydrocarbons or ethers. Very preferred solvents
are selected from pentane, hexane, heptane, ligroin, petroleum ether (benzene), cyclohexane,
dichloromethane, trichloromethane, tetrachloromethane, benzene, toluene, xylene, chlorobenzene,
dichlorobenzene, dibutylether, tetrahydrofuran, dioxane and mixtures thereof.
[0113] Esterification can be carried out in the absence or presence of an inert gas. The
term "inert gas" refers to gas which does not react with the educts, reagents, solvents
or the products formed in the reaction under the given process conditions. Preferably,
esterification is carried out without the addition of an inert gas.
[0114] Optionally, the 2,5-furandicarboxylic acid ester which was thus obtained can be further
purified by drying and filtering.
[0115] In another preferred embodiment, the reaction between the 2,5-furandicarboxylic acid
and the mixture of the at least one branched or linear, substituted or unsubstituted
aliphatic C6 to C20 alcohol of the general formula R-OH can be preferably carried
out using stochiometric amounts of 2,5-furandicarboxylic acid and alcohol based on
the number of reactive OH- and CO
2H-groups, particularly when entrainers are used.
[0116] However, one preference can be optionally given to using a stochiometric excess (based
on the number of reactive OH- and CO
2H-groups) of the alcohol component of from 0.05 to 1.0 mole per mole of 2,5-furandicarboxylic
acid component in order to achieve complete conversion of 2,5-furandicarboxylic acid.
[0117] In another preferred manner, the esterification reaction between 2,5-furandicarboxylic
acid and the at least one alcohol is carried out in two stages, wherein already in
the first stage substantial amounts of the desired 2,5-furandicarboxylic acid ester
are formed without the addition of a catalyst, preferably at least one of the catalysts
as described above. The temperatures to be employed in this first stage depend largely
on the starting materials. Satisfactory reaction rates are achieved above 100°C, and
preferably above 120°C. It is possible to already complete the carboxylic ester formation
at these temperatures.
[0118] However, it is more advantageous to increase the temperature continuously up to 160
°C. When using 2,5-furandicarboxylic acid (rather than the corresponding carboxylic
anhydride thereof) as the esterification component, the water formed is removed from
the reaction system as an azeotrope with the alcohol, as long as the reaction temperature
is above the boiling point of the azeotrope (i.e. in a range from 90°C to 100°C under
atmospheric pressure). The course and completion of the esterification can in this
case be observed via the formation of water. The use of subatmospheric or superatmospheric
pressure is not ruled out, but is rather restricted to special cases. To suppress
the occurrence of concentration differences, it is advisable to stir the reactor contents
or to mix them from time to time, e.g. by passing an inert gas through the reaction
mixture.
[0119] It is further optional to work up the formed 2,5-furandicarboxylic acid ester by
filtration, optionally followed by distillation.
[0120] In the second stage, the esterification of the 2,5-furandicarboxylic acid is completed.
The second stage is carried out in the presence of catalysts at temperatures which
are above those employed in the first stage and go up to 250°C. Water formed during
the reaction is removed as an azeotrope, with the alcohol acting as an entrainer.
[0121] After completion of the reaction, the reaction mixture comprises not only the desired
reaction product, but it may still contain 2,5-furandicarboxylic acid together with
excess alcohol and the catalyst.
[0122] To work up the crude 2,5-furandicarboxylic acid ester, the product from the reactor
is first neutralized with alkali metal hydroxide or alkaline earth metal hydroxide.
The alkaline reagent is employed as an aqueous solution containing from 5 to 20 percent
by weight, preferably from 10 to 15 percent by weight, of the hydroxide, based on
the overall weight of the solution.
[0123] The amount of neutralizing agent to be used depends on the proportion of acid components,
free acid and 2,5-furandicarboxylic acid ester in the crude product. The use of the
selected hydroxides, among which sodium hydroxide has been found to be particularly
useful, as aqueous solution having a particular concentration and in a defined excess
ensures that the acidic constituents of the reaction mixture are precipitated in a
crystalline, very readily filterable form.
[0124] At the same time, the catalyst is largely decomposed to form likewise easily filterable
products. The alkaline treatment of the crude 2,5-furandicarboxylic acid ester is
not tied to the maintenance of particular temperatures. It is advantageously carried
out immediately after the esterification step without prior cooling of the reaction
mixture.
[0125] Subsequently any free alcohol is separated from the reaction mixture. Steam distillation
has been found to be useful for this step and can be carried out in simple form by
passing steam into the crude product.
[0126] The removal of the free alcohol is typically followed by the drying of the 2,5-furandicarboxylic
acid ester. In a particularly simple and effective embodiment of this step, drying
is achieved by passing an inert gas through the product. The crude 2,5-furandicarboxylic
acid ester is then filtered to free it of solids. The filtration is carried out in
conventional filtration equipment at room temperature or at temperatures up to 150°C.
The filtration can also be facilitated by customary filter aids such as cellulose
or silica gel.
[0127] Alternatively to the esterification process described above for preparing the 2,5-furandicarboxylic
acid esters to be used as lubricants in the present invention, transesterification
can also be applied.
[0128] The conventional processes known to the person skilled in the art can be used for
the transesterification, e.g. a process that involves the reaction of a di-ester of
2,5-furandicarboxylate, preferably as prepared by the esterification process described
above, with at least one branched or linear, substituted or un-substituted aliphatic
C6 to C20 alcohol of the general formula R-OH in the presence of at least one suitable
transesterification catalyst, like preferably a titanium(IV) alcoholate.
[0129] Transesterification catalysts that can be used are the conventional catalysts usually
used for transesterification reactions, where these are mostly also used in esterification
reactions. Among these are by way of example mineral acids, such as sulfuric acid
and phosphoric acid; organic sulfonic acids, such as methanesulfonic acid and p-toluenesulfonic
acid; and specific metal catalysts from the group of the tin(IV) catalysts, for example
dialkyltin dicarboxylates, such as dibutyltin diacetate, trialkyltin alkoxides, monoalkyltin
compounds, such as monobutyltin dioxide, tin salts, such as tin acetate, or tin oxides;
from the group of the titanium catalysts: monomeric and polymeric titanates and titanium
chelates, for example tetraethyl orthotitanate, tetrapropyl orthotitanate, tetrabutyl
orthotitanate, triethanolamine titanate; from the group of the zirconium catalysts:
zirconates and zirconium chelates, for example tetrapropyl zirconate, tetrabutyl zirconate,
triethanolamine zirconate; and also lithium catalysts, such as lithium salts, lithium
alkoxides; and aluminum(III) acetylacetonate, chromium(III) acetylacetonate, iron(III)
acetylacetonate, cobalt(II) acetylacetonate, nickel(II) acetylacetonate, and zinc(II)
acetylacetonate.
[0130] The amount of transesterification catalyst used is from 0.001 to 10% by weight, preferably
from 0.05 to 5% by weight. The reaction mixture is preferably heated to the boiling
point of the reaction mixture, the reaction temperature therefore being from 20°C
to 200°C, depending on the reactants.
[0131] The transesterification can take place at ambient pressure or at reduced or elevated
pressure. It is preferable that the transesterification is carried out at a pressure
of from 0.001 to 200 bar, particularly from 0.01 to 5 bar. The relatively low-boiling-point
alcohol eliminated during the transesterification is preferably continuously removed
by distillation in order to shift the equilibrium of the transesterification reaction.
The distillation column necessary for this purpose generally has direct connection
to the transesterification reactor, and it is preferable that said column is a direct
attachment thereto. If a plurality of transesterification reactors is used in series,
each of said reactors can have a distillation column, or the vaporized alcohol mixture
can preferably be introduced into a distillation column from the final tanks of the
transesterification reactor cascade by way of one or more collection lines. The relatively
high-boiling-point alcohol reclaimed in said distillation is preferably returned to
the transesterification.
[0132] If an amphoteric catalyst is used, this is generally removed via hydrolysis and subsequent
removal of the resultant metal oxide, e.g. via filtration. It is preferable that,
after reaction has been completed, the catalyst is hydrolyzed by means of washing
with water, and the precipitated metal oxide is removed by filtration. The filtrate
can, if desired, be subjected to further work-up for the isolation and/or purification
of the product. It is preferable that the product is isolated by distillation.
[0133] The transesterification of the di-ester of 2,5-furandicarboxylic acid preferably
takes place in the presence of the alcohol component and in the presence of at least
one titanium(IV) alcoholate. Preferred titanium(IV) alcoholates are tetrapropoxytitanium,
tetrabutoxytitanium, and mixtures thereof. It is preferable that the amount used of
the alcohol component is at least twice the stochiometric amount, based on the di-ester
of the 2,5-furandicarboxylic acid used.
[0134] The transesterification can be carried out in the absence of, or in the presence
of, an added organic solvent. It is preferable that the transesterification is carried
out in the presence of an inert organic solvent. Suitable organic solvents are those
mentioned above for the esterification. Among these are specifically toluene and THF.
[0135] The transesterification is preferably carried out in the temperature range from 50
to 200°C.
[0136] The transesterification can take place in the absence of or in the presence of an
inert gas. The expression inert gas generally means a gas which under the prevailing
reaction conditions does not enter into any reactions with the starting materials,
reagents, or solvents participating in the reaction, or with the resultant products.
It is preferable that the transesterification takes place without addition of any
inert gas.
[0137] One particularly suitable embodiment of the transesterification process comprises:
- a) reaction of 2,5-furandicarboxylic acid with methanol in the presence of concentrated
sulfuric acid to give dimethyl 2,5-furandicarboxylate,
- b) reaction of the dimethyl 2,5-furandicarboxylate obtained in step a) with at least
one branched or linear, substituted or un-substituted aliphatic C6 to C20 alcohol
of the general formula R-OH in the presence of at least one titanium(IV) alcoholate
to give the desired 2,5-furandicarboxylic acid esters to be used as lubricants in
the present invention.
[0138] The 2,5-furandicarboxylic acid ester to be used as lubricant in the present invention
as well as the lubricant compositions according to the present invention comprising
the inventive2,5-furandicarboxylic acid ester can be favourably used for various applications.
[0139] One preferred application are as components in engine oils. Such general applications
includes all sorts of engine oils, including light, medium and heavy duty engine oils,
industrial engine oils, marine engine oils, crankshaft oils, compressor oils, refrigerator
oils, hydrocarbon compressor oils, very low-temperature lubricating oils and fats,
high temperature lubricating oils and fats, wire rope lubricants, textile machine
oils, refrigerator oils, aviation and aerospace lubricants, aviation turbine oils,
transmission oils, gas turbine oils, spindle oils, spin oils, traction fluids, transmission
oils, plastic transmission oils, passenger car transmission oils, truck transmission
oils, industrial transmission oils, industrial gear oils, insulating oils, instrument
oils, brake fluids, transmission liquids, shock absorber oils, heat distribution medium
oils, transformer oils, fats, chain oils, metalworking operations in general, particularly
as minimum quantity lubricants for metalworking operations, oil to the warm and cold
working, oil for water-based metalworking liquids, oil for neat oil metalworking fluids,
oil for semi-synthetic metalworking fluids, oil for synthetic metalworking fluids,
drilling detergents for the soil exploration, hydraulic oils, in biodegradable lubricants
or lubricating greases or waxes, chain saw oils, release agents, moulding fluids,
gun, pistol and rifle lubricants or watch lubricants and food grade approved lubricants.
[0140] In preferred embodiments, the 2,5-furandicarboxylic acid esters of the present invention
are used in lubricant compositions, in particular the 2,5-furandicarboxylic acid esters
are used in lubricant compositions in automatic transmission fluids, manual transmission
fluids, hydraulic fluids, grease, gear fluids, crankcase engine oils, shock absorber
fluids, industrial oils, metal-working fluids, transformer oils, biodegradable lubricants
and seal plasticizing agents.
[0141] At least 40 mole percent of the 2,5-furandicarboxylic acid, preferably at least 50
mole percent, more preferably at least 65 mole percent, even more preferably at least
75 mole percent, and most preferably at least 85 mole percent of the 2,5-furandicarboxylic
acid, and sometimes even at least 90 mole percent, or at least 95 mole percent or
even 100 mole percent are hereby derived from a renewable source.
[0142] In a preferred use, the 2,5-furandicarboxylic acid ester is obtained by esterification
of the 2,5-furandicarboxylic acid, preferably of the 2,5-furandicarboxylic acid of
at least partial renewable origin, with a mixture of Guerbet alcohols as defined herein,
which is a mixture that was obtained from the Guerbet reaction. In another preferred
embodiment of the present invention, this mixture of Guerbet alcohols is also at least
partially derived from a renewable source.
[0143] Accordingly, one very preferred use is directed to the use of the 2,5-furandicarboxylic
acid of at least partial, preferably full, renewable origin with a mixture of Guerbet
alcohols of at least partially, preferably fully, renewable origin for the preparation
of 2,5-furandicarboxylic acid ester of at least partially, preferably fully, renewable
origin.
[0144] The 2,5-furandicarboxylic acid esters obtained from esterification of 2,5-furandicarboxylic
acid and at least one branched or linear, substituted or unsubstituted aliphatic C6
to C20 alcohol, like a mixture of Guerbet alcohols as described herein, allow the
preparation of lubricant compositions with attractive rheological performance characteristics,
favourable viscosity profiles, good hydrolytic and oxidative stability, good seal
compatibility and favourable traction behaviour.
[0145] Consequently, the lubricant compositions of the present invention due to the presence
of the 2,5-furandicarboxylic acid ester have excellent hydrolytic and oxidative stability,
good seal performance, and attractive rheological performance characteristics, like
kinematic viscosity profile, over a very broad temperature range, and favourable traction
behaviour when compared with other lubricants that are based on different carboxylic
acid esters. Similarly, the latter performance characteristics of known lubricant
compositions can be further improved by the addition, or supplementation of the 2,5-furandicarboxylic
acid ester of the present invention.
[0146] The lubricant compositions of the present invention comprising the 2,5-furandicarboxylic
acid esters have kinematic viscosity at 40°C as determined by ASTM D 445 in the range
of from 90.0 to 160.0 mm
2/s, preferably 100.0 to 150.0 mm
2/s, and more preferably 110.0 to 140.0 mm
2/s. Most preferred are values in the range of from 120.0 to 135.0 mm
2/s.
[0147] The lubricant compositions of the present invention comprising the 2,5-furandicarboxylic
acid esters have kinematic viscosity at 100°C as determined by ASTM D 445 in the range
of from 5.0 to 30.0 mm
2/s, preferably 10.0 to 25.0 mm
2/s, and more preferably 12.0 to 20.0 mm
2/s. Most preferred are values in the range of from 15.0 to 18.0 mm
2/s.
[0148] The lubricant compositions of the present invention comprising the 2,5-furandicarboxylic
acid esters have viscosity index as determined by ASTM D 2270 in the range of from
125 to 160, preferably 130 to 155, and more preferably from 140 to 150.
[0149] The lubricant compositions of the present invention comprising the 2,5-furandicarboxylic
acid esters have pour point as determined by ISO 3016 in the range of from -70°C to
-40°C, preferably from -65°C to -45°C and more preferably from -60°C to -50°C.
[0150] The lubricant compositions of the present invention comprising the 2,5-furandicarboxylic
acid esters have cloud point as determined by ISO 3015 in the range of from -100 to
-65, preferably - 90 to -70, and more preferably from -85 to -75.
[0151] The lubricant compositions of the present invention comprising the 2,5-furandicarboxylic
acid esters also have good oxidation stability and hydrolytic stability.
[0152] The following examples illustrate the invention without being intended to limit the
invention thereto.
Examples
General procedure for the synthesis of diester
[0153] To a 2-L round bottom flask fitted with a Dean-Stark apparatus were added 6.00 mol
(4.0 eq.) of the respective alcohol (
n-octanol, 2-ethyl hexanol or 2-propyl heptanol) and 500 g toluene. 2-Propylheptanol
is commercially available from BASF SE, Ludwigshafen and represents a mixture of 93.0
wt.-% 2-propyl-heptanol, 2.9 wt.-% 2-propyl-4-methyl-hexanol, 3.9 wt.-% 2-propyl-5-methylhexanol
and 0.2 wt.-% 2-isopropylheptanol. The stirred mixture was heated to reflux (114-155
°C) and 234 g (1.50 mol, 1.0 eq.) 2,5-furandicarboxylic acid were added followed by
11.5 g (0.12 mol, 8 mol-%) 99.9% sulfuric acid in 3 or 4 equal portions whenever conversion
slowed. The conversion was monitored by the amount of water deposited in the Dean-Stark
apparatus. Upon complete conversion a sample was drawn and submitted to GC analysis.
The cooled reaction mixture was transferred to a separatory funnel and washed twice
with 500 mL saturated NaHCO
3 solution (upon addition of the alkaline NaHCO
3 solution vigorous CO
2 formation may result). The organic phase was washed with brine, dried over anhydrous
NaSO
4 and the solvents were removed under reduced pressure. The crude products were purified
by fractioning or vacuum distillation or precipitation. The purity and identity of
the compounds was determined by GC(-MS) and/or NMR analysis. GC-columns: Agilent J&W
DB-5, 30 m x 0,32 mm x 1,0 µm or Ohio Valley OV-1701 60 m x 0,32 mm x 0,25 µm).
[0154] 2-Ethylhexyl-2,5-furandicarboxylate was obtained in 76 % yield and 95.7 % purity
2-Propylheptyl-2,5-furandicarboxylate was obtained in 58 % yield and 97.8 % purity.
2-Octyl-2,5-furandicarboxylate was obtained in 75 % yield and 98.7 % purity.
[0155] Characterization of the diester 2-propylheptyl-2,5-furandicarboxylate
|
Units |
Methods |
Result |
|
Kinematic viscosity at 40°C |
mm2/s |
ASTM D 445 |
47.7 |
|
Kinetic viscosity at 100°C |
mm2/s |
ASTM D 445 |
5.9 |
|
Viscosity index |
|
ASTM D 2270 |
46 |
|
Pour point |
°C |
ISO 3016 |
-48 |
|
Cloud point |
°C |
ISO 3015 |
<-70 |
|
Noack volatility |
% |
ASTM D5800B |
9.3 |
|
Hydrolytic stability |
mg KOH/g |
SS155181 |
0 h |
0.76 |
Total acid number |
|
|
120 h |
1.45 |
|
|
|
196 h |
2.02 |
[0156] It was found that 2-propylheptyl-2,5-furandicarboxylate was highly viscous while
at the same time showing a low pour point. Moreover, 2-propylheptyl-2,5-furandicarboxylate
is both hydrolytically and thermally stable.
[0157] The following inventive lubricant composition comprising the 2,5-furandicarboxylic
acid ester was prepared and characterized:
Lubricant composition 1 |
wt.-% |
Diester of 2-propylheptyl 2,5-furandicarboxylate (>98,5%) |
10.0 |
Base oil (Synfluid, PAO-6) |
52.0 |
Viscosity modifier, PIB (Lubrizol® 8406, from Lubrizol) |
13.0 |
Viscosity modifier, OCP (Lubrizol® 8407, from Lubrizol) |
13.0 |
Additive package (Anglamol 6004, available from Lubrizol) |
12.0 |
Characterization of lubricant composition 1 |
Kinematic viscosity at 40°C (mm2/s) |
ASTM D 445 |
130,83 |
Kinematic viscosity at 100°C (mm2/s) |
ASTM D 445 |
17,668 |
Viscosity index |
ASTM D 2270 |
149 |
Water content (%) |
ASTM E 203 |
0,15 |
Cloud Point °C |
ISO 3015 |
-80 |
Pour Point °C |
ISO 3016 |
-54 |
[0158] The lubricant composition showed a favorable viscosity profile over a broad range
of temperatures while having a low pour point at the same time.