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Effect of the Fluid Viscosity

RPM and Piston Configuration of Performance of Controlled-Clearance Deadweight Tester

by D.H. Newhall, V.A. Zilberstein, and I. Ogawa*

*I. Ogawa was not of Harwood Engineering Company, Inc., but rather from Tokyo Electron Limited, Tokyo, Japan
Controlled-clearance deadweight testers [1-4] are used widely as the primary pressure standards above the manometer level. Our recent experimental studies have shown [5] that the fluid viscosity is an important consideration in evaluation of the effective area, since it affects float and stall curve slopes. Experiments were made on DWT-300 and DWT-1000 with various fluids such as white gasoline, light turbine oil DTE-24, Univis P12 and Spin-Esso in a wide range of pressures up to 1.4 GPa.

It is shown (Figure 1) that the stall curves, i.e. stall jacket pressure-measured pressure curves, for more viscous fluids, such as a synthetic ester base oil P12, or DTE24 oil, and for "low viscosity" fluid, namely white gasoline, do not coincide, though, conceptually, one would expect it to be a single line. This finding is contradictory to what was previously generally believed. Thus a choice of fluid for DWT becomes a very vital problem. It will require both serious practical and theoretical considerations in order to improve overall accuracy of DWT operating on more viscous fluids.

Experimental results on the slopes of float curves plotted Figure 2 in the coordinates measured pressure — cube root of the fall rate provide information which is shown to be sufficient to estimate viscosity of the fluids under pressure or, at least their piezocoefficient of viscosity. We estimated viscosity of white gasoline at room temperature from our results obtained for a DWT-1000 at pressures up to 1.4 GPa (Figure 3).

For evaluation of the viscosity in this pressure range we used the following relation:

m = xm³Pm
where x is a constant largely dependent on geometry and material properties of the piston and cylinder, m the slope of a fall-rate curve, Pm the measured pressure. The fall-rate curve slope was described empirically on the basis of experimental data. The constant x was found by using a boundary condition that the viscosity at 1.1 GPa should be the same as found recently [6] for white gasoline in a high-pressure falling-body viscometer. Since the falling body data were obtained in the range from 1.1 to 2.1 GPa there was some overlap between the DWT and viscometry data. Curvature of the viscosity-pressure curve changes in the vicinity of 1 GPa where the viscosity amounts to about 0.1 Pa·s. According to our data, viscosity of white gasoline at room temperature changes by seven orders of magnitude when pressure is increased from normal to 2.1 GPa (Figure 3). The viscosity at atmospheric pressure measured by Brookfield Laboratories was 4.5 x 10-4 Pa·s.

DWT-1000 was run at various RPM, typically 0, 8, 16, 35, 80, and 160. Surprisingly we found a significant effect of RPM on the performance of the DWT in the range 0-35 RPM. The nature of the effect is yet to be studied. From a practical point of view, determination of an optimum RPM versus sensitivity of the instrument is highly desirable.

Until recently only plain cylindrical pistons (Figure 4a) were used in DWT. Alternate configurations were made (spherical [7] and grooved Figure 4b and c) and tested to .14 GPa in the DWT-1000. These pistons allowed variation in the pressure gradient length and in the location along the cylinder of the point where the pressure drops to atmospheric. It is shown that with oil these pistons behave well indicating their potential for further studies of pressure gradient effects. However, preliminary studies using white gasoline showed the spherical and grooved pistons to be extremely sensitive to minute changes in jacket pressure and to the relative positioning of the piston and cylinder, resulting in poor reproducibility of the fall rate data with low viscosity fluids. These alternate configurations appear promising as research tools as well as practical new conceptions of piston-cylinder arrangements.

Footnotes

1 U.S. Patent 2,796,229 (1949).
2 D.P. Johnson and D.H. Newhall, Trans. ASME 75, 301-310 (1953).
3 C.O. Bennett and B. Vodar, High Pressure Measurement, ed. by A.A. Giardini and E.C. Lloyd (Butterworths, Washington, 1963), p. 365.
4 P.L.M. Heydemann and B.E. Welch, Experimental Thermodynamics, ed. by B. Leneindre and B. Vodar (Butterworths, London, 1975), Vol. 2, Chap. 4, Part 3, p. 147.
5 D.H. Newhall, I. Ogawa and V.A. Zilberstein, Review Scientific Instruments, 50 (August 1979).
6 L.H. Abbot, D.H. Newhall, V.A. Zilberstein, and J.F. Dill, to be presented at the joint ASME-ASLE Conference, Dayton, Ohio, Oct. 1979.
7 U.S. Patent 3,630,071.

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