A circular cylinder is one of the basic geometrical shapes and the flow passing over it can be simulated by combination of a uniform flow and doublet. When the distance between source-sink pair approaches zero, the shape Rankine oval becomes more blunt and approaches a circular shape.
Consider the superposition of a uniform flow of velocity
and a doublet of
strength
as shown in Fig. The
direction of the doublet is upstream, facing into uniform flow.

Fig. : Superposition of a uniform flow and doublet.
The stream function for the combined flow is,
![]() |
1 |
The velocity field is obtained as,
![]() |
2 |
In order to locate the stagnation point, assign the velocity
components in Eq.2 to zero value and simultaneously solve for
. There are two
stagnation points, located at
and
denoted by points A and B, respectively. The equation of
streamlines that passes through the stagnation points A and B, is
given by the following expression;
![]() |
(3) |
This equation is satisfied by
for all values of θ.
Since R is a constant, Eq. (3) may be interpreted as the equation
of a circle with radius R with center at the origin. It is
satisfied by
for all values of
R. Different values of R may be obtained by varying the uniform
velocity and/or doublet strength. Hence, entire horizontal axis
through the points A and B, extending infinitely far upstream and
downstream, is a part of stagnation streamline. The above
discussions can be summarized as follows;
• The dividing streamline is a circle of radius R. The family of circles can be obtained by assigning different values of R with various doublet strength and free stream velocity.
• The flow inside the circle is generated from the doublet whereas flow outside the circle comes from the uniform flow. So, the flow inside the circle may be replaced by solid body and the external flow will not feel the difference.
• Thus, the inviscid, irrotational, incompressible flow over a
circular cylinder of radius R can be simulated by adding a uniform
flow of velocity
and a doublet of
strength
and R is related to
AND
.
|
|
(4) |
that passes through
the stagnation points A and B as shown in Fig. 1.Referring to the Fig. 1, it is seen that the entire flow field is symmetrical about both horizontal and vertical axes through the center of the cylinder. It means the pressure distribution is also symmetrical about both the axes. When the pressure distribution over the top part of the cylinder is exactly balanced by the bottom part, there is no lift . Similarly, when the pressure distribution on the front part of the cylinder is exactly balanced by rear portion, then there is no drag. This is in contrast to the realistic situation i.e. a generic body placed in a flow field will experience finite dragand zero lift may be possible. This paradox between the theoretical result of zero drag in an inviscid flow and the knowledge of finite drag in real flow situation is known as d' Alembert's paradox .
Pressure Coefficient
In general, pressure is a dimensional quantity. Many a times, it is expressed in a non-dimensional form with respect to free stream flow and the ‘pressure coefficient' is defined as follows;
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|
Here,
are the free stream
density and free stream velocity, respectively. The term
is called as dynamic
pressure. For incompressible flow, if a body is immersed in the
free stream, then Bernoulli's equation can be written at any
arbitrary point in the flow field as,
![]() |
(6) |
On the surface of the cylinder
shown in Fig. 1, the
velocity distribution can be obtained from Eq. (2) i.e.
![]() |
(7) |

Fig. 2: Maximum velocity in the flow over a circular cylinder.
Here,
is geometrically
normal to the surface and
is tangential to the
surface of the cylinder as shown in Fig. 2(a). The negative sign
signifies that
is positive in the
direction of increasing θ. It may be observed that the velocity at
the surface reaches to maximum value of
at the top and
bottom of the cylinder as shown in Fig. 2(b). Eqs. (6) and (7) can
be combined to obtain the surface pressure coefficient as,
![]() |
(8) |
The pressure distribution over the cylinder is plotted in Fig.
3. Here,
varies from 1 at the
stagnation point to -3 at the points of maximum velocity. It is
also clear that the pressure distribution at the top half the
cylinder is equal to the bottom half and hence the lift is zero.
Similarly, the pressure distribution on the front part of the
cylinder is exactly balanced by rear portion and there is no drag.
Both, normal force and axial force coefficients
are same as lift and
drag coefficients. They are calculated from
as given below;
![]() |
(9) |
Here, LE and TE stands for leading edge and trailing edge, respectively. The subscripts u and lrefers to upper and lower surface of the cylinder. The chord c is the diameter of the cylinder (R).

Fig. 3: Surface pressure coefficient for a circular cylinder.
When the surface pressure matches with free stream pressure, then Eq. (3.7.8) reduces to,
![]() |
(10) |
These points as well as the stagnation points and location of minimum pressure are illustrated in Fig. 4.

Fig. 4: Pressure values at various locations on the surface of the cylinder.
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