Long-Term Trends in Industrial Lubricant Additives 617
oils in such a way that they will be compatible with antiwear additives containing ZDDP so that no
precipitates that could plug lters are formed [12].
Test methods have been developed to evaluate the thermal and hydrolytic stability of antiwear
hydraulic oils. Test method ASTM D 2070 evaluates the thermal stability of an oil by heating the
test oil in the presence of copper and iron rods for 168 h at 135°C. At the end of the test, the metal
rods are rated by visual examination and the sludge is isolated by ltration and weighed. Test method
ASTM D 2619 evaluates hydrolytic stability by heating and agitating the test oil with water and a
copper strip in a sealed glass bottle for 48 h at 93°C. At the end of the test, the viscosity change of
the oil and the acidity changes of the oil and the water phases are measured, the weight loss of the
copper strip is determined, and any resulting insoluble material is isolated and weighed.
24.3.2.4 Metal Deactivators
Owing to the potential corrosiveness of the decomposition products of the antiwear additives, the
presence of an effective metal deactivator is even more important in antiwear hydraulic oils than in
turbine oils. Table 24.3 lists the types of metal deactivators that can be used in hydraulic oils.
24.3.2.5 Foam Inhibitor
Because air is compressible, foam or entrained air interferes with the primary function of a hydraulic
oil, which is to transfer power. Therefore, the type and amount of silicone or polyacrylate antifoam
additive must be carefully chosen to maximize foam inhibition while maintaining good air release
properties. Some original equipment manufacturers are extremely concerned about the presence
of silicone materials in their plants as it is believed that even a trace of silicone on a metal surface
can affect paint coating properties. Therefore, these manufacturers require that only nonsilicone
antifoam additives be used in lubricating oils employed in their plants.
The choice of antifoam additive may also be affected by the practice of hydraulic oil condition
monitoring. Often, optical particle counters based on light scattering techniques are used to monitor
oil cleanliness. As antifoam additives are nely dispersed, partially insoluble uids in oil, they can
falsely be registered as particles by some optical particle counters. In the future, one criterion for
choosing antifoam additives may be their ability to disperse suf ciently so as not to interfere with
the function of optical particle counters.
24.3.2.6 Viscosity Index Improver
VI improvers are used to widen the useful operating temperature range of hydraulic oils. They are long-
chain polymers that function by uncoiling or dissociating at elevated temperatures, resulting in thicken-
ing of the oil. Owing to this property, oils containing VI improvers will display higher measured kinetic
viscosities at elevated temperatures than comparable oils that have the same 40°C oil viscosity but do
not contain VI improver. The types of polymers used as VI improvers are listed in Table 24.3.
An important property of VI improvers for hydraulic oils is shear stability. If a VI improver
lacks shear stability, it will quickly be degraded by the hydraulic pump and will lose its ability to
increase the viscosity of the base oil at elevated temperatures. This will result in less-than-optimum
lubricant lm thickness and accelerated pump wear. Generally, the shear stability of VI improvers
increases as the molecular weight decreases. However, the thickening capability of the VI improver
also decreases as the molecular weight decreases. A trend in the industry is to use VI improv-
ers with better shear stability for better pump protection. Therefore, lower-molecular-weight VI
improvers are used although they must be used at higher percentages by weight.
One method for determining the shear stability of hydraulic oil containing a VI improver,
ASTM D 5621, is based on sonic irradiation. In this method, a sample of test oil is irradiated in a
sonic oscillator for a speci ed time interval and the change in viscosity after shear is determined.
It is claimed that the amount of shear measured by this method is similar to the amount of shear
imparted to a hydraulic oil in a hydraulic vane pump test [20].
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