This paper describes the high-pressure
volumetric properties of
three commonly used poly(α-olefin) base oilsPAO 2, PAO
4, and PAO 8with nominal 100 °C kinematic viscosities
of 2, 4, and 8 cSt. Using a special variable-volume view cell that
permits continuous pressure scan and volume measurements, densities
were determined at 298, 323, 348, 373, and 398 K at pressures up to
40 MPa. Isothermal compressibilities, isobaric thermal expansivities,
thermal pressure coefficients, and internal pressures were then evaluated.
At each temperature, density–pressure correlations were developed
for the range from 10 to 40 MPa. Density–temperature correlations
were developed at 10, 20, 30, and 40 MPa. It is shown that the densities
of PAO 2 (which were in the range from 0.7364 to 0.8214 g/cm3) are lower than those of PAO 4 (in the range from 0.7663 to 0.8470
g/cm3) or PAO 8 (in the range from 0.7664 to 0.8498 g/cm3). The densities of PAO 4 and 8 were essentially the same.
Isothermal compressibilities of each base oil were of the same order
of magnitude at each temperature (with the range being from 6.8 to
10.2 × 10–4 MPa–1), with
PAO 2 showing slightly higher values. Isobaric thermal expansivities
were in the range (7.2–9.5) × 10–4 K–1. PAO 2 showed higher expansivity values at all pressures.
Thermal pressure coefficients were in the range 0.8–1.2 MPa
K–1. The values were higher for PAO 2 at 323 K and
higher temperatures. PAO 8, while showing the highest thermal pressure
coefficient at 298 K, became lower than that of PAO 2 at 323 K and
lower than that of PAO 4 at 348 K and higher temperatures. At 398
K, PAO 4 shows the highest thermal pressure coefficients. The trends
observed with the thermal pressure coefficients were also reflected
in the internal pressures for the respective oils. The internal pressure
values were in the range from 260 to 370 MPa. The internal pressure
value in each system was observed to decrease with pressure. These
observations were interpreted in terms of the differences in the carbon
chain lengths, ease of packing, and relative significance of attractive
versus repulsive forces that develop as a function of the pressure
or temperature.
Temperature and pressure effects
on density and viscosity are reported
for six base oils consisting of four mineral oils and two synthetic
oils composed of poly(α-olefins). Using a variable-volume view
cell, density data were collected at 298, 323, 348, 373, and 398 K
from 10 to 40 MPa. The data were then fit to the Sanchez–Lacombe
equation of state and used to determine isothermal compressibility,
isobaric thermal expansion coefficient, and internal pressure. Compressibility
and internal pressure were found to vary based on composition, specifically
with cycloalkane content. Viscosity data were collected as a function
of temperature, pressure, and rotational speed using a custom-built
high pressure rotational viscometer. Data were collected at 298, 323,
348, and 373 K from 10 to 40 MPa at rotational speeds of 300–800
rpm. A free-volume model was used to model the viscosity and relate
the viscous effects to density.
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