872 ENGINEERING THERMODYNAMICSdharm
\M-therm\Th16-1.pm5Substituting the value of M 02 in eqn. (16.18), we getps = p 0 +pV
p0020 M M
002 04
2
1
42
24γρ
γ
×++F −γ +
HGI
KJor, ps = p 0 +ργ 002 02
2 1 4 042
24VMF ++− M +
HGI
KJ... ...(16.19)Also, ps = p 0 +
ρ 002
2V
(when compressibility effects are neglected) ...(16.20)
The comparison of eqns. (16.19) and (16.20) shows that the effects of compressibility are
isolated in the bracketed quantity and that these effects depend only upon the Mach number. The
bracketed quantity ie. ., 1 M M ...
4
2
240
2
0F ++− (^4) +
HG
I
KJ
L
N
M
M
O
Q
P
P
γ may thus be considered as a compressibility
correction factor. It is worth noting that :
l For M < 0.2, the compressibility affects the pressure difference (ps – p 0 ) by less than 1 per cent
and the simple formula for flow at constant density is then sufficiently accurate.
l For larger value of M, as the terms of binomial expansion become significant, the
compressibility effect must be taken into account.
l When the Mach number exceeds a value of about 0.3 the Pitot-static tube used for
measuring aircraft speed needs calibration to take into account the compressibility
effects.
16.6.2. Expression for stagnation density (ρs)
From eqn. (ii), we haveρ
ρ00 γ1ssp
p
=
F
HGI
KJor
ρ
ρssp γ
00 p1
=
F
HGI
KJor ρs = ρ 0
p
ps
01
F
HGI
KJγSubstituting the value ofp
ps
0F
HGI
KJ from eqn. (iv), we getρs = ρ 0 1 1
2 02 11+F −
HGI
KJR
S
TU
V
WL
N
M
M
MO
Q
P
P
Pγ −γ
γγ
Mor, ρs = ρ 0 1
1
2 021
1
+
F −
HGI
KJL
N
MO
Q
Pγ γ−
M ...(16.21)16.6.3. Expression for stagnation temperature (Ts)
The equation of state is given by :p
ρ = RT
For stagnation point, the equation of state may be written as :
ps
ρs
= RTs or Ts =1
Rps
ρs