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Vaporization of JP-8 Jet Fuel in a Simulated Aircraft Fuel Tank ...

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higher altitudes, as cont<strong>in</strong>uous sampl<strong>in</strong>g with the high flow sample pump would cause<br />

false read<strong>in</strong>gs by the FID due to air enter<strong>in</strong>g the ullage through the vents, and cont<strong>in</strong>uous<br />

sampl<strong>in</strong>g with the FID’s built-<strong>in</strong> pump would not draw enough sample for the FID to<br />

give accurate read<strong>in</strong>gs. Therefore, the comparison was performed at sea level, where the<br />

cont<strong>in</strong>uous sampl<strong>in</strong>g with the FID’s built-<strong>in</strong> pump was known to be accurate.<br />

The two tests were <strong>in</strong>tended to be identical, but varied slightly due to different<br />

<strong>in</strong>itial conditions. Figure 5.9 compares the liquid fuel temperatures and measured vapor<br />

concentrations for the two tests. Consider<strong>in</strong>g the differences between the test conditions<br />

for the two tests, there is good agreement between the two methods <strong>of</strong> ullage vapor<br />

sampl<strong>in</strong>g, <strong>in</strong>dicat<strong>in</strong>g that m<strong>in</strong>or difference is noticed between <strong>in</strong>termittent and cont<strong>in</strong>uous<br />

ullage vapor sampl<strong>in</strong>g; thus, <strong>in</strong>termittent sampl<strong>in</strong>g can be used <strong>in</strong> lieu <strong>of</strong> cont<strong>in</strong>uous<br />

sampl<strong>in</strong>g when necessary.<br />

Liquid Temperature, Deg. F.<br />

140<br />

120<br />

100<br />

80<br />

60<br />

40<br />

20<br />

0<br />

Thermocouple<br />

Error<br />

FID Error<br />

Liquid Temp<br />

Measured THC<br />

Calculated THC, 115 FP<br />

Calculated THC, 120 FP<br />

0 500 1000 1500 2000 2500 3000<br />

Time, seconds<br />

Figure 5.6. <strong>JP</strong>-8 fuel vaporization at sea-level, constant ambient pressure and temperature;<br />

comparison <strong>of</strong> calculated and measured ullage vapor concentration, M.L. =31.5kg/m 3 .<br />

3<br />

2.5<br />

2<br />

1.5<br />

1<br />

0.5<br />

0<br />

% Propane Equivalent<br />

38

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