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CURRENT NEEDS AND DEVELOPMENTS IN
HYDRAULIC FLUID TECHNOLOGIES
George E. Totten' and John V. Sherman2
1. G.E. Totten and Associates, Inc., Stony Point, NY USA (GETotten @ aol.com)2. BASF Inc., Wyandotte, MI USA (shermaj @basf.com)
ABSTRACT
There are various governmental and industry pressures on the fluid power industry that necessitates substantial
improvements in fluids and materials used in the fluid power industry. For example, substantial improvements in
fluid lifetimes, especially oxidative stability at higher use temperatures and dramatic improvements inbiodegradability and toxicity for mineral oil fluids is vital. Another very important and continuing market and
technology thrust in the fluid power industry is in the development of alternative hydraulic fluids whose
performance will rival that of petroleum oil. Substantial improvements in the materials used in hydraulic systemswith respect to corrosion and antiwear performance is vital. In fact, it is impossible further ignore the fact thatthe hydraulic fluid must be considered as a design component of the hydraulic system. This itself is a relatively
recent focal point. An overview of these and other technology thrusts will be discussed. The focus of this
discussion will be on the development of biodegradable fluids.
KEYWORDS
Hydraulic fluids, biodegradability, antiwear, design
INTRODUCTIONPetroleum oil basestocks are highly complex
chemical mixtures whose composition,biodegradability and toxicity vary with the crude oilsource [1]. Although petroleum oils havetraditionally been the most commonly usedhydraulic fluids in the fluid power industry, they arebeing subjected to ever-increasing controlsparticularly due to the increasingly stringentgovernmental regulations regarding the impact ofhydraulic fluid spill and fluid leakage on theenvironment.[2] Improper disposal, even if it isincidental, may be the source of large penalties oreven litigation.[3]
Hydraulic fluid leakage has been identified as a
potential source of ground water contamination [4].Such concerns have led to a world-wide effort toidentify hydraulic fluids, which will exhibit reducedenvironmental and toxicological impact uponincidental contact with the environment [5,6].Specific industries where these environmentalconcerns are particularly important includeagricultural [7], forestry [8] and other off-highwayapplications [9]. (Note: The term "environmentalimpact" includes biodegradation, persistence andtoxicity.)
This report will provide a selected review ofvarious aspects of biodegradable fluid technology.
DISCUSSION
Biodegradable Fluids
Thus far, the most commonly cited base
stocks used for the formulation of "environmentally
friendly" hydraulic fluids are either vegetable oils
or synthetic esters [ 10,11,12]. Polyalphaolefin
basestock has also been shown to be biodegradable
[13].
The most common vegetable oils that have
been identified for hydraulic fluid formulations are:
canola oil [14], soybean oil, [15,16,17] rapeseed
oil [18], and high oleic sunflower oil [19].
Rapeseed oil and canola oil are common vegetable
oil basestocks for formulation of biodegradable
hydraulic fluids [20]. Canola oil derived hydraulic
fluids have been successfully used in Germany as
long as the bulk fluid temperatures were kept below
60•Ž.[21]
Soybean oil, because it is readily
available in the USA, is also being evaluated as a
basestock for hydraulic fluid formulation
[15,16,22-26]. Studies completed to date have
shown that soybean oil derived hydraulic fluids
exhibit excellent performance in various
commercial and agricultural applications.[27]
Another class of biodegradable fluid basestocks
that have been reported are polyol esters and diesters.
[14,28] The molecular structure of the fluid
Fluid Power.Fifth JFPS International Symposium (C) 2002 JFPS.ISBN4-931070-05-3
395
basestock will dictate the end-use performance
properties. For example, Konishi, et. al. have
reported the effect of diester structure on properties
such as co-efficient of friction and elastomer
compatibility [29].
The biodegradability properties of fire-resistant
hydraulic fluids including phosphate esters [30] and
water-glycols [31,32,33] have been reported but will
not be detailed here.
In addition to the basestock, a hydraulic fluid
typically contains additives. Additives are used to
enhance fluid properties which include: oxidative
stability, antiwear, reduced foaming and improved air
release properties. The presence of these additives
also affect hydraulic fluid biodegradation and
toxicological properties [34-37] . In many cases,
additives used for petroleum oil formulations [1] are
unsuitable, therefore since additive selection will
affect biodegradability. [38]. additives developed
specifically for use with biodegradable basestocks
must be used [38,39].
Physical Properties
To perform satisfactorily as a pressure medium
in a hydraulic system, the fluid must exhibit at least
targeted minimum physical properties. For example,
the fluid must exhibit acceptable flash point, air
release, foaming and demulsibility properties.
However, there are some properties that are
particularly critical and have been difficult for
biodegradable, particularly vegetable oil-based and
ester-based fluids, to achieve and maintain during use.
These properties include: hydrolytic stability,
oxidative stability, corrosion protection, desired
traction coefficients and seal compatibility.
Low Temperature Properties
Low temperature properties of biodegradable
hydraulic fluids, especially pour point and low
temperature stability are important, especially in
mobile equipment operation in cold weather. In
many end-use machinery applications, such as
forestry, hydraulic fluids are subjected to widely
varying operating temperatures from-35•Ž (-310F)
to 100•Ž (2120F) and operating pressures up to 450
bar (6500 psi)[7]. A viscosity index of at least 150 is
desired [40]. Typically, increasing molecular weight
of the acid and ester functional moieties will degrade
low temperature performance.
Omeis [41] and Konishi [42] have shown that
branched diesters exhibit significantly improved low
temperature performance. Increased branching
improves low temperature performance.[43]
Rhee, et. al. have shown that synthetic esters
exhibit a number of advantages over vegetable oils
such as a broader pour point temperature range,
typically, -40•Ž-150•Ž versus vegetable oil derived
fluids which typically exhibit a temperature range of
-10•Ž-90•Ž [44,45,46]. Without the use of additives,
many vegetable oils fractionally crystallize some of
the saturated derivatives at approximately -10-
-20•Ž .[47] This more limited range of operational
temperatures for vegetable oils often renders them
unsuitable for cold-weather applications.
Oxidative Stability
Hydraulic fluids used in off-highway
applications are often subjected to higher
temperatures than encountered in stationary
applications. Therefore, oxidative stability is
particularly important. The oxidative stability of
vegetable-based fluids is directly related to oleic
acid content. Increasing oleic acid content, relative
to di-and tri-unsaturated acids, provides
corresponding increases in oxidative stability
[25,26,48] . However, the oxidative stability for
fluids with increased oleic acid content is still often
insufficient and therefore are often only suitable for
restricted use [27,49]. In some cases, recommended
use temperatures of 60•Ž [28]-80•Ž [22] have
been reported or if used at higher temperatures, a
reduced oil change interval is recommended [22].
The amount of unsaturation in a vegetable oil is
climate-dependent [19]. Increasing amounts of
unsaturation results in increasingly less oxidatively
stable fluids [34]. For example, rapeseed grown in
colder northern climates contains less unsaturation
(canola oil) than when grown in warmer southern
climates. This is important because the level of
unsaturation affects physical properties, especially
oxidative stability [13,28]. This means that the
performance of vegetable oils as hydraulic fluid
basestocks is inherently variable.
Remmelmann and Murrenhoff have studied
the oxidative stability of biodegradable fluids using
the Rotary Bomb Oxidation Test (RBOT)
according to the ASTM D 2272 test procedure. In
this study, it was shown that oxidative stability,
while only minimally affected by water
contamination, was significantly affected by the
presence of some metals such as copper [47].
Interestingly, catalytic levels of iron exhibited
a much smaller catalytic effect. The presence of
iron and copper arise from corrosion [43].
Fortunately, biodegradable iron and copper
corrosion inhibitors are commercially available
[40]. The effect of water content on oxidative
stability was examined in detail by Remmelmann
and Murrenhoff [47].
In addition to the well known RBOT (ASTM
D 2272) test, the Baader test, modified IP 48 and a"dry" TOST (ASTM D 943) test have also been
used to evaluate oxidative stability of vegetable oils
and synthetic esters.[28,44,51 ](The test must be
run dry to avoid hydrolysis of the ester
functionality.) The dry TOST test has the
disadvantages of relatively large sample sizes (300
mL) and long testing times (2000 h).[28]
396
Alternatively, a high-pressure differential scanningcalorimetry (HP-DSC) test may be used for rapidscreening.
Currently, polyol ester and diester-basedfluids are being promoted as more oxidatively
stable biodegradable basestocks than vegetable oil-based fluids [14,41,52]. The degree ofimprovement in oxidative stability is dependent onthe antioxidant seleced [28].
Hydrolytic StabilityIn mobile hydraulics applications, it is difficult
to exclude the possibility of moisture (water)contamination. Sources of water ingression into thesystem include: water contamination of fresh fluid,rain water entrance into the reservoir, storage inunsealed containers, unprotected breathers, improper
filling techniques, and moisture contamination bycontact with humid air [43]. In the presence oforganic esters such as vegetable oils and syntheticesters, this is a problem since esters hydrolyze,
particularly in the presence of a catalyst, to formorganic acids [40,47].
The generation of acidic by-products exhibit anumber of deleterious effects including: catalysis ofthe hydrolysis reaction and corrosion enhancement
[40]. Interestingly, water contamination of vegetableoils and synthetic esters exhibits only a minimaleffect on oxidative instability as shown in Figure 8
[41]. However, this was due to reduced hydraulicload since the system pressure and temperature werereduced to minimize excessive hydraulic wear.
Since hydrolytic instability cannot be controlled,water contamination must either be eliminated or itmust be removed before hydrolysis occurs [51].Recently, a redesigned reservoir which utilizes theheat from the fluid to volatilize water into theatmosphere was reported [43]. Generally, it isrecommended that water levels < 500 ppm bemaintained [52] although water levels of 100 200
ppm may be achieved using the modified reservoirdesign [43].
Corrosion PropertiesThe use of yellow metals (copper alloys) is a
common type of material used in construction ofrunning surfaces in high pressure hydraulic pumps
[53] . For example, yellow metals may be used forpiston slippers and the running surfaces of thecylinder barrel and valve plate or bushing. One
potential failure mode of hydraulic pumps usingvegetable oils and synthetic esters is corrosion ofthese yellow metal surfaces. It has been shown thesulfur, either organic or inorganic, containingvegetable oils exacerbated corrosion of yellow metalsurfaces [22,40,41].
Krauss, et.al. have described the developmentof the "Linde Test" which is used as a screening testfor yellow metal corrosion under both static and
dynamic conditions [54]. The "Static Linde Test" is
conducted by heating different materials for 100
hours in the biodegradable fluid at 120•Ž, 10%
mineral oil, and 1% water. The materials that are
screened are: steel, cast iron, brass, cast bronze, and
sintered bronze with different levels of tin.
Observation and comparison determine the relative
amounts of corrosion. The limitation of this test is
that it does not account for the type of corrosion and
the stability of the corroded layer.
The apparatus used for the "Dynamic Linde
Test" includes a thermostatically controlled hot plate,
and test container. The test fluid is 89% ester, 10%
mineral oil and 1% water and glass beads. Four test
specimens; brass, cast bronze, sintered bronze and
hardened bearing steel are mounted on the stirrer.
The stirrer is rotated at 200 rpm and the fluid is
maintained at 120•Ž for 100 h. After the test, the
weight loss is determined as g/m2 of surface area.
Although excellent correlations with field tests
were obtained, it was concluded that field tests were
still necessary to validate the final results of these
screening processes.
Elastomer Compatibility
Elastomer compatibility with biodegradable
fluids has been examined by a number of authors
[40,41,55]. Although nitrile rubbers (NBR) are
among the most commonly used materials with
petroleum oil fluids, they are generally incompatible
with various types of biodegradable fluids [41,55]. In
general, only fluoroelastomers and some
polyurethane materials are compatible with
biodegradable fluids above 80•Ž [40,55]. However,
since compatibility varies with each fluid-elastomer
combination and use condition, compatibility must
be assessed on an individual basis.
Lubrication Properties
The antiwear behavior of biodegradable
hydraulic fluids is typically determined in two steps.
The first is to obtain a preliminary assessment using a
bench test such as: FZG (DIN 51 354) [40], 4-ball
wear (ASTM D 4172) [40], flywheel testing
[38,49,80], Aachen twin disk test [41,47], oscillating
pin-on-plate test [42], or a Plint and Partner High
Frequency Friction Machine (TE 77B), using two
different contact geometries; a cylinder-on-plate and
ball-on-disk [39]. Typically excellent antiwear results
were obtained with formulated biodegradable fluids,
however, lower viscosity ester basestocks exhibited
somewhat higher coefficients of friction than did
longer-chain, higher molecular weight esters [40].
Mineral oil-based fluids exhibited higher coefficients
of friction than obtained with various biodegradable
fluids examined [29,42,47].
The best fluid candidates were screened by
hydraulic pump testing. In addition to testing with
Vickers V-104 vane pump (DIN 51 389)[40], other
397
hydraulic pumps have also been used including:Vickers 35VQ25 vane pump [39], KomatsuHPV35+35 axial piston pump [22, 41], Sauer-Sundstrand Series 90 axial piston pump [49],Mannesmann Rexroth A4 VSG 125 axial piston
pump, and others [58] Although the antiwear resultswere generally good, these tests showed thatvegetable oils exhibit poorer oxidative stability thanmineral oil based hydraulic fluids.
FiltrationSince it would be difficult to perform in-
line filtration without restricting the fluid flow in thesystem, off-line filtration is typically used [52, 59].When converting from petroleum oil to abiodegradable oil, precipitate formation is oftenencountered. The precipitate typically contains metalcontaminants due to the additives originally presentin the petroleum oil. The presence of this precipitateresults in significantly reduced filter life. However,this problem has been corrected with the use of ahybrid filter as an alternative to more commonlyencountered paper filters in an off-line configuration
[59]. In this way, It is possible to maintain ISO 16/12or better using off-line filtration [52].
CONCLUSIONSAlthough mineral oil based hydraulic fluids
exhibit some of the best overall properties, they havetwo significant deficiencies; fire resistance andbiodegradability which may preclude their continueduse in many applications. While there is little thatcan be done about the poor fire resistance of mineraloils, except engineering or hardware modifications,bviodegradability may be improved. In generalhydrogen reduction or removal of aromatic
compounds and increasing the overall parafiniccomposition will improve aquatic biodegradability,
but not to vegetable oil or synthetic ester levels.
However, even highly refined mineral oilcompositions are among the most persistent in soil
biodegradability tests.Two biodegradable alternatives to mineral oil
based hydraulic fluids are vegetable oils and
synthetic esters. They are more biodegradable than
mineral oil. Of the two basestocks, vegetable oils are
somewhat more biodegradable although that dependssomewhat on molecular structure. In soil tests,
vegetable oils are clearly more biodegradable. One
vegetable oil, sunflower oil, although biodegradable,
exhibited significant toxicity to seedling growth andyield.
Polyol esters, usually those based on trioleateesters of trimethylolpropane, exhibit excellentthermal stability relative to vegetable oils.Formulated fluids, although exhibiting excellentbiodegradability, exhibit relatively poor soilbiodegradability, a notable disadvantage in additionto their relatively higher cost.
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