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Basics of Fluid Mechanics, 2014a

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11.4. ISENTROPIC FLOW 401<br />

Table -11.1. Fliegner’s number and other parameters as function <strong>of</strong> Mach number (continue)<br />

M Fn ˆρ<br />

(<br />

P 0 A ∗<br />

AP<br />

) 2<br />

RT 0<br />

P 2<br />

( ṁ<br />

) 2 1<br />

A Rρ 0P<br />

( ṁ<br />

) 2 1<br />

A Rρ 2 0 T<br />

( ṁ<br />

) 2<br />

A<br />

0.95 2.188 1.843 3.181 10.88 6.112 4.037<br />

0.96 2.233 1.881 3.259 11.60 6.436 4.217<br />

0.97 2.278 1.920 3.338 12.37 6.777 4.404<br />

0.98 2.324 1.961 3.419 13.19 7.136 4.600<br />

0.99 2.371 2.003 3.500 14.06 7.515 4.804<br />

1.00 2.419 2.046 3.583 14.98 7.913 5.016<br />

Example 11.10:<br />

A gas flows in the tube with mass flow rate <strong>of</strong> 0.1 [kg/sec] and tube cross section is<br />

0.001[m 2 ]. The temperature at chamber supplying the pressure to tube is 27 ◦ C. At<br />

some point the static pressure was measured to be 1.5[Bar]. Calculate for that point<br />

the Mach number, the velocity, and the stagnation pressure. Assume that the process<br />

is isentropic, k =1.3, R = 287[j/kgK].<br />

Solution<br />

The first thing that need to be done is to find the mass flow per area and it is<br />

ṁ<br />

A =0.1/0.001 = 100.0[kg/sec/m2 ]<br />

It can be noticed that the total temperature is 300K and the static pressure is 1.5[Bar].<br />

It is fortunate that Potto-GDC exist and it can be just plug into it and it provide that<br />

M<br />

T<br />

T 0<br />

ρ<br />

ρ 0<br />

A<br />

A ⋆<br />

P<br />

P 0<br />

A×P<br />

A ∗ ×P 0<br />

F<br />

F ∗<br />

0.17124 0.99562 0.98548 3.4757 0.98116 3.4102 1.5392<br />

The velocity can be calculated as<br />

U = Mc= √ kRTM =0.17 × √ 1.3 × 287 × 300× ∼56.87[m/sec]<br />

The stagnation pressure is<br />

P 0 =<br />

P<br />

P/P 0<br />

=1.5/0.98116 = 1.5288[Bar]<br />

End Solution<br />

11.4.6 Isentropic Tables

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