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602 Chapter 11 ■ Compressible Flow<br />

From Eq. 1 we obtain<br />

V 10.4992 23386 1ft # lb21lbm # °R241488 °R211.662<br />

279 1ft # lblbm2 1 2<br />

or, using 1 lb 32.2 lbm # fts 2 ,<br />

V 279 1ft # lblbm2 1 2 3132.2 lbm # fts 2 2lb4 1 2<br />

1580 fts<br />

(Ans)<br />

isentropic flow along a pathline in a stagnation process. Even<br />

though these equations and graph were developed for onedimensional<br />

duct flows, they can be used for frictionless, adiabatic<br />

pathline flows also.<br />

Furthermore, while the Mach numbers calculated above are of<br />

similar size for the air and helium flows, the flow speed is much<br />

larger for helium than for air because the speed of sound in helium<br />

is much larger than it is in air.<br />

COMMENT Note that the isentropic flow equations and Fig.<br />

D.1 for k 1.4 were used presently to describe <strong>fluid</strong> particle<br />

The ratio of flow<br />

area to the critical<br />

area is a useful<br />

concept for isentropic<br />

duct flow.<br />

Also included in Fig. D.1 is a graph of the ratio of local area, A, to critical area, A*, for different<br />

values of local Mach number. The importance of this area ratio is clarified below.<br />

For choked flow through the converging–diverging duct of Fig. 11.6a, the conservation of<br />

mass equation 1Eq. 11.402 yields<br />

or<br />

From Eqs. 11.36 and 11.46, we obtain<br />

and<br />

rAV r*A*V*<br />

A<br />

A* ar* r b aV* V b<br />

V* 1RT*k<br />

V Ma 1RTk<br />

By combining Eqs. 11.67, 11.68, and 11.69 we get<br />

A<br />

A* 1 Ma ar* b a r 0<br />

r 0 r b 1T*T 0 2<br />

B 1TT 0 2<br />

The incorporation of Eqs. 11.56, 11.60, 11.63, 11.65, and 11.70 results in<br />

A<br />

A* 1 Ma e 1 31k 12 24Ma 2<br />

1 31k 1224<br />

1k12 321k124<br />

f<br />

(11.67)<br />

(11.68)<br />

(11.69)<br />

(11.70)<br />

(11.71)<br />

Equation 11.71 was used to generate the values of AA* for air 1k 1.42 in Fig. D.1. These values<br />

of AA* are graphed as a function of Mach number in Fig. 11.10. As is demonstrated in the<br />

following examples, whether or not the critical area, A*, is physically present in the flow, the area<br />

ratio, AA*, is still a useful concept for the isentropic flow of an ideal gas through a converging–<br />

diverging duct.<br />

2.0<br />

A ___<br />

A*<br />

1.0<br />

0 1.0<br />

Ma<br />

F I G U R E 11.10 The variation of area<br />

ratio with Mach number for isentropic flow of an<br />

ideal gas ( k 1.4, linear coordinate scales).

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