The dynamic viscosities of four high-viscous
vacuum oil samples,
working liquids (BM-1CM, BM-1CN, LEYBONOL LVO 500, and Alkaren-D24)
for diffusion vacuum pumps, have been measured over the temperature
range from 298 to 443 K at atmospheric pressure. The measurements
were made using a newly designed rheoviscometer based on falling-body
and capillary flow techniques. A new design of the rheoviscometer
can be used to measure the viscosity of high and extra-high-viscous
working liquids (Newtonian) and rheological properties (non-Newtonian
liquids) at low temperatures (near the melting temperature). The present
design of the rheoviscometer has some advantage over conventional
viscometers. For example, it allows us to measure the viscosity of
high and extra-high viscous liquids (Newtonian) and rheological properties
of non-Newtonian liquids by changing the shear stress. The combined
expanded uncertainty of the viscosity, atmospheric pressure, and temperature
measurements at the 0.95 confidence level with a coverage factor of k = 2 is estimated to be U
r(η)
= 2.8%, U
r(P) = 0.01,
and U(T) = 0.02 K, respectively.
For verification of the reliability, accuracy, and correct operation
of the newly designed rheoviscometer, the viscosity of the same oil
samples were measured using a conventional well-known capillary flow
viscometer over the temperature range from 293 to 366 K at atmospheric
pressure. The measured viscosity data for vacuum oils were used to
estimate physical meaning parameters of the modified (extended) Arrhenius–Andrade
and Vogel–Tamman–Fulcher (VTF) models. The derived VTF
parameters (Band T
0,
δ = B/T
0) were
used to estimate the values of the glass temperature for studied vacuum
oil samples.