878 ENGINEERING THERMODYNAMICSdharm
\M-therm\Th16-1.pm5Throat
A=A 21Fig. 16.7. Sonic flow (M = 1).Large tankConvergent
nozzle2
V 2
p, ,T 222 rp 1r 1T 1V=0 11V<V
p>p
>
T>T21
21
21
21rrV>V
p<p
<
T<T21
21
21
21rr
V 1 V 2 V 1 V 2( ) Divergent nozzle.a ( ) Convergent nozzle.b
Fig. 16.6. Supersonic flow (M > 1).
(iii)For sonic flow (M = 1) :
dA
A = 0 (straight flow passage
since dA must be zero)
and dp = (zero/zero) i.e., indeterminate, but
when evaluated, the change of pressure
p = 0, since dA = 0 and the flow is fric-
tionless.16.8. Flow of Compressible Fluid Through a Convergent Nozzle
Fig. 16.8 shows a large tank/vessel fitted with a
short convergent nozzle and containing a compressible
fluid. Consider two points 1 and 2 inside the tank and
exit of the nozzle respectively.
Let p 1 = pressure of fluid at the point 1,
V 1 = velocity of fluid in the tank (= 0),
T 1 = temperature of fluid at point 1,
ρ 1 = density of fluid at point 1, and p 2 , V 2 , T 2 and
ρ 2 are corresponding values of pressure, velocity, tem-
perature and density at point 2.
Assuming the flow to take place adiabatically,
then by using Bernoulli’s equation (for adiabatic flow),
we have
γ
γρ−F
HGI
KJ
+
121
11
p^2
gV
g + z^1 =γ
γρ−F
HGI
KJ
+
122
22
p^2
gV
g + z^2 [Eqn. (16.7)]
But z 1 = z 2 and V 1 = 0∴γ
γρ− 11
1p
g =γ
γρ−F
HGI
KJ+
122
22
p^2
gV
gor,γ
γ−F
HGI
1 KJ^p
gp
g1
12
ρρ 2
−L
NM
O
QP =
V
g22
2or
γ
γ− 1pp 1
12
ρρ 2−
L
NM
O
QP V^2
2
2Fig. 16.8. Flow of fluid through a
convergent nozzle.