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Fuels & Lubricants Magazine

Issue No. 3, October 2018

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mm 2 /s, authors [4] attempted to extrapolate<br />

the coefficient α to other oil<br />

viscosities as well. The results are on<br />

Pictures 4 and 5. Picture 4 shows the<br />

correlation between viscosity-pressure<br />

coefficient α and kinematic<br />

viscosity of these oils at 200 MPa.<br />

Picture 5 shows the same correlation<br />

at 600 MPa. Both charts are valid for<br />

the temperature range 25 – 80 °C.<br />

Figure 4: Pressure coefficient at 200 MPa<br />

N - naphtenic oil<br />

SI - silicone oil<br />

M - paraffinic mineral oil<br />

PAO - polyalfaolefine oil<br />

ES - ester oil<br />

PG - polyalkyleneglycol oil<br />

MPa are PG, Ester or PAO synthetic<br />

oils. Paraffinic mineral oil is worse<br />

and naphtenic is the worst.<br />

All these oils were measured the<br />

same way as paraffinic mineral oil<br />

in Figure 3, but as there are not any<br />

data about solidification, it is issued<br />

only brief description based of high<br />

viscosity measurement.<br />

The best was polyglycol oil with<br />

KV40°C = 100 mm 2 /s. Its viscosity<br />

400 000 mPa.s was reached at 500<br />

MPa for oil temperature 26.8 °C.<br />

The pressure 800 MPa increased<br />

the viscosity only to 20 000 mPa.s at<br />

70.2 °C. The worst was silicone oil<br />

with KV 40 °C = 120 mm 2 /s, which<br />

reached viscosity 400 000 mPa.s<br />

already at half pressure than PG oil<br />

– at 250 MPa (and at 26.8 °C). The<br />

higher temperature = 70.1 °C improves<br />

its behaviour to get viscosity<br />

400 000 mPa.s at 430 MPa.<br />

Following the Picture 3 it is possible<br />

to estimate the curve of paraffinic<br />

mineral oil with KV40 °C = 9.62<br />

mm 2 /s. The shape and slope of this<br />

curve will be similar as the curve belongs<br />

to the temperature 37 °C, but<br />

the starting point is shifted down to<br />

10 1 mPa.s, it can be calculated more<br />

exactly as 8.40 mPa.s. The solidification<br />

point deducted from the chart is<br />

at 520 MPa.<br />

Figure 5: The same chart for 600 Mpa<br />

Literature Data Discussion<br />

The lowest viscosity-pressure<br />

coefficient at normal conditions (see<br />

Picture 4) shows very low viscosity<br />

silicone oil, but there are doubts<br />

about its very high pressure behavior,<br />

especially when higher viscosity<br />

silicone oils have really enormous<br />

steep slope of viscosity-pressure<br />

relationship. This is strange, because<br />

generally all other oils show<br />

the higher is viscosity index, the<br />

lower is coefficient α. It is confirmed<br />

by Stepina [2] as well. Maybe the<br />

structure based on Si-O exhibit<br />

different relationship. Nevertheless<br />

the lubricating properties of low<br />

viscosity silicone oil or even silicone<br />

solvent are poor and that is why it is<br />

impossible to recommend it for this<br />

expensive apparatus.<br />

Following the Picture 5 the best<br />

candidates for the range of temperatures<br />

25 °C – 80 °C and pressure 600<br />

Data Comparison and<br />

Evaluation<br />

The temperature of actually used<br />

transformer oil was 30 °C, kinematic<br />

viscosity was 13.7 mm 2 /s (12.0<br />

mPa.s) at that temperature. Solidification<br />

Point from the chart (Figure 3)<br />

is at 490 MPa, if it would be paraffinic<br />

oil. See Figure 6. As the transformer<br />

oil is naphtenic origin, then lower<br />

pressure can be expected to cause<br />

solidification. 420 – 460 MPa is expected<br />

pressure which cause solidification<br />

of transformer oil at 30 °C.<br />

This value is in a very good agreement<br />

with experiment. The pressure<br />

interval between 420 – 500 MPa is<br />

caused by increasing temperature<br />

<strong>Fuels</strong>&<strong>Lubricants</strong> No. 3 OCTOBER 2018 7

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