451An Introduction to Two-Dimensional Compressible Flow
Similarly,
=
T
yc
p
y
p
1
ρ
(14.23)
Substituting Equations 14.22 and 14.23 into Equations 14.20 and 14.21, respectively, gives
+
+
=
x
uv
C
T
x
p
22
2
0
i.e., since c
p
is assumed constant,
+
+
=
x
cT
uv
p
22
2
0
(14.24)
and
+
+
=
y
cT
uv
p
22
2
0
(14.25)
These two equations together indicate that the quantity
cT
uv
p
+
+
22
2
remains constant in an irrotational isentropic ow. This is the same as the result deduced
from energy considerations. Thus, in irrotational isentropic ow, momentum, and energy
conservation considerations give the same result. This was discussed in Chapter 4.
The Velocity Potential
The equations governing the velocity eld in two-dimensional irrotational ow are the
continuity equation (14.2) and the irrotationality equation (14.19), i.e.,
Equation 14.2:
+
=
x
u
y
v() ()
ρρ
0
452 Introduction to Compressible Fluid Flow
Equation 14.19:
=
v
x
u
y
0
The boundary conditions on these equations are that u and v are prescribed in the initial
ow, e.g., u = u
, v = 0 well upstream of the body considered, and that the velocity compo-
nent normal to any solid surface is zero.
If a quantity, Φ, termed the velocity potential, is introduced, Φ being such that
u
x
v
y
=
=
ΦΦ
,
(14.26)
then it will be seen that the left-hand side of Equation 14.19 becomes
∂∂
∂∂
22
ΦΦ
xy
yx
This will always be zero so it follows that the velocity potential function, as dened by
Equation 14.26, satises the irrotationality equation (14.19). The continuity equation (14.2)
must then be used to solve for Φ. This equation gives
+
=
xx yy
ρρ
ΦΦ
0
i.e.,
ρ
ρρ
+
+
+
=
2
2
2
2
0
ΦΦ ΦΦ
xy
xx yy
(14.27)
However, since isentropic ow is being considered,
ρ=Cp
1
γ
(14.28)
Hence,
=
=
=
ρρ
x
Cp
p
p
xp
p
x
a
p
x
11
1
2
γγ
γ
Similarly, it can be shown that
=
ρ
y
a
p
y
1
2
(14.29)
453An Introduction to Two-Dimensional Compressible Flow
Using these in the momentum equations (14.5) and (14.6) and using Equation 14.26, then
gives
=−
+
∂∂
ρρ
x
a
x
x
yxy
2
2
2
2
ΦΦ
ΦΦ
(14.30)
and
=−
∂∂
+
ρρ
y
a
xxyy
y
2
22
2
ΦΦ
ΦΦ
(14.31)
Substituting these two equations into Equation 14.27 then gives
+
+
2
2
2
22
2
2
2
2
1ΦΦ ΦΦΦΦ Φ
xya
x
x
xy
xxy
a
yxxy y
∂∂
+
1
2
2
2
2
ΦΦ ΦΦΦΦ
=
y
2
0
i.e.,
+
+
2
2
2
22
2
2
2
2
1
2
ΦΦ ΦΦΦΦ Φ
xya
x
x
xy
∂∂
+
=
xy y
y
ΦΦ
2
2
2
0
(14.32)
This can be written as
+
+
∂∂
+
2
2
2
22
2
2
2
2
2
2
2
1
2
ΦΦ ΦΦΦ
xya
u
x
uv
xy
v
y
= 0
(14.33)
Beside Φ, this equation contains the speed of sound a. An expression relating a to Φ is
therefore required. This is supplied by the energy equation, which, as discussed above,
gives (see Equation 14.14)
cT
uv
cT
pp
+
+
=
22
0
2
(14.34)
where T
0
is the stagnation temperature, which is a constant throughout the ow. Hence,
since
a
2
= γRT and C
p
= γR/(γ 1)
454 Introduction to Compressible Fluid Flow
Equation 14.34 gives
au
va
222
0
2
1
20
+
+=
γ
()
i.e., using Equation 14.26,
aa
xy
2
0
2
2
2
1
2
=−
+
γ
Φ
Φ
(14.35)
Equations 14.32 and 14.35 together describe the variation of Φ in irrotational, isentropic,
ow. In low-speed ow (i.e., M 1), the density variation is negligible and Equation 14.27
gives
+
=
2
2
2
2
0
ΦΦ
xy
(14.36)
Hence, in low-speed ow, the variation of Φ is governed by Laplace’s equations. In
incompressible ow, then, it is relatively easy to determine Φ, Equation 14.36 being a linear
equation. In compressible ow, however, the compressibility effects give rise to the nonlin-
ear terms in Equation 14.32, i.e., terms such as (∂Φ/∂x)
2
(∂
2
Φ/∂x
2
), which involve the product
of functions of Φ. This makes the determination of Φ in compressible ows signicantly
more difcult than in incompressible ows. To solve for Φ in compressible ows, the fol-
lowing methods can be used:
• Full numerical solutions
• Transformation of variables to give a linear governing equation
• Linearized solutions
The second method is only applicable in a few situations and will not be discussed here.
Linearized solutions will be discussed in the next section and a very brief discussion of
numerical methods is given in a later section.
Linearized Solutions
To keep the drag low on objects in high-speed ows, the objects are usually kept relatively
slender to minimize the disturbance they produce in the ow. With such slender objects,
the differences between the values of the ow variables near the object and the values of
these variables in the freestream ow ahead of the object are small, e.g., consider the situ-
ation shown in Figure 14.8.
455An Introduction to Two-Dimensional Compressible Flow
If the components in the x- and y-directions of the velocity V are u
+ u
p
and v
p
then, for
a slender object, the perturbation velocities u
p
and v
p
will be very small compared with u
.
This assumption is the basis for the analysis given in the present section.
Now, in the undisturbed ow ahead of the object, u = u
and v = 0, so the velocity poten-
tial is, by virtue of Equation 14.26, given by
=
=
ΦΦ
x
u
y
an
d0
i.e.,
Φ = u
x
The velocity potential in the ow will therefore be written as
Φ = u
x + Φ
p
where Φ
p
is the perturbation velocity potential, which must be such that
u
x
v
y
p
p
p
p
=
=
ΦΦ
, (14.37)
Substituting the above relations into the potential function equation in the form given
in Equation 14.33 leads to
+
−+
++
∞∞
2
2
2
22
2
2
2
2
1
2
ΦΦ Φ
pp
p
p
pp
xya
uu
x
uuv() ()
Φ
ΦΦ
p
p
p
xy
v
y
∂∂
+
=
2
2
2
0
i.e.,
+
+
+
2
2
2
2
2
2
2
2
1
ΦΦ Φ
pp pp
xy
u
a
u
u
x
221
2
2
2
+
∂∂
+
∞∞
u
u
v
uxy
v
u
pp pp
Φ ΦΦ
p
y
=
2
0
(14.38)
V
y
x
u
v
= 0
FIGURE 14.8
Flow situation considered.

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