878 ENGINEERING THERMODYNAMICS
dharm
\M-therm\Th16-1.pm5
Throat
A=A 21
Fig. 16.7. Sonic flow (M = 1).
Large tank
Convergent
nozzle
2
V 2
p, ,T 222 r
p 1
r 1
T 1
V=0 1
1
V<V
p>p
>
T>T
21
21
21
21
rr
V>V
p<p
<
T<T
21
21
21
21
rr
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
HG
I
KJ
+
12
1
1
1
p^2
g
V
g + z^1 =
γ
γρ−
F
HG
I
KJ
+
12
2
2
2
p^2
g
V
g + z^2 [Eqn. (16.7)]
But z 1 = z 2 and V 1 = 0
∴
γ
γρ− 1
1
1
p
g =
γ
γρ−
F
HG
I
KJ
+
12
2
2
2
p^2
g
V
g
or,
γ
γ−
F
HG
I
1 KJ^
p
g
p
g
1
1
2
ρρ 2
−
L
N
M
O
Q
P =
V
g
22
2
or
γ
γ− 1
pp 1
1
2
ρρ 2
−
L
N
M
O
Q
P V^2
2
2
Fig. 16.8. Flow of fluid through a
convergent nozzle.