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Section 3
3.6 External Incompressible Flows
Alan T. McDonald
Introduction and Scope
Potential ßow theory (Section 3.2) treats an incompressible ideal ßuid with zero viscosity. There are no
shear stresses; pressure is the only stress acting on a ßuid particle. Potential ßow theory predicts no drag
force when an object moves through a ßuid, which obviously is not correct, because all real ßuids are
viscous and cause drag forces. The objective of this section is to consider the behavior of viscous,
incompressible ßuids ßowing over objects.
A number of phenomena that occur in external ßow at high Reynolds number over an object are
shown in Figure 3.6.1. The freestream ßow divides at the stagnation point and ßows around the object.
Fluid at the object surface takes on the velocity of the body as a result of the no-slip condition. Boundary
layers form on the upper and lower surfaces of the body; ßow in the boundary layers is initially laminar,
then transition to turbulent ßow may occur (points ÒTÓ).
FIGURE 3.6.1 Viscous ßow around an airfoil (boundary layer thickness exaggerated for clarity).
Boundary layers thickening on the surfaces cause only a slight displacement of the streamlines of the
external ßow (their thickness is greatly exaggerated in the Þgure). Separation may occur in the region
of increasing pressure on the rear of the body (points ÒSÓ); after separation boundary layer ßuid no
longer remains in contact with the surface. Fluid that was in the boundary layers forms the viscous wake
behind the object.
The Bernoulli equation is valid for steady, incompressible ßow without viscous effects. It may be
used to predict pressure variations outside the boundary layer. Stagnation pressure is constant in the
uniform inviscid ßow far from an object, and the Bernoulli equation reduces to
p¥ +
1 2
rV = constant
2
(3.6.1)
where p¥ is pressure far upstream, r is density, and V is velocity. Therefore, the local pressure can be
determined if the local freestream velocity, U, is known.
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Fluid Mechanics
Boundary Layers
The Boundary Layer Concept
The boundary layer is the thin region near the surface of a body in which viscous effects are important.
By recognizing that viscous effects are concentrated near the surface of an object, Prandtl showed that
only the Euler equations for inviscid ßow need be solved in the region outside the boundary layer. Inside
the boundary layer, the elliptic Navier-Stokes equations are simpliÞed to boundary layer equations with
parabolic form that are easier to solve. The thin boundary layer has negligible pressure variation across
it; pressure from the freestream is impressed upon the boundary layer.
Basic characteristics of all laminar and turbulent boundary layers are shown in the developing ßow
over a ßat plate in a semi-inÞnite ßuid. Because the boundary layer is thin, there is negligible disturbance
of the inviscid ßow outside the boundary layer, and the pressure gradient along the surface is close to
zero. Transition from laminar to turbulent boundary layer ßow on a ßat plate occurs when Reynolds
number based on x exceeds Rex = 500,000. Transition may occur earlier if the surface is rough, pressure
increases in the ßow direction, or separation occurs. Following transition, the turbulent boundary layer
thickens more rapidly than the laminar boundary layer as a result of increased shear stress at the body
surface.
Boundary Layer Thickness Definitions
Boundary layer disturbance thickness, d, is usually deÞned as the distance, y, from the surface to the
point where the velocity within the boundary layer, u, is within 1% of the local freestream velocity, U.
As shown in Figure 3.6.2, the boundary layer velocity proÞle merges smoothly and asymptotically into
the freestream, making d difÞcult to measure. For this reason and for their physical signiÞcance, we
deÞne two integral measures of boundary layer thickness. Displacement thickness, d*, is deÞned as
¥
d*
=
d
æ
u ö æ yö
ò è1 - U ø d è d ø
(3.6.2)
0
FIGURE 3.6.2 Boundary layer on a ßat plate (vertical thickness exaggerated for clarity).
Physically, d* is the distance the solid boundary would have to be displaced into the freestream in a
frictionless ßow to produce the mass ßow deÞcit caused by the viscous boundary layer. Momentum
thickness, q, is deÞned as
q
=
d
ò
¥
0
y
uæ
u
1 - ö dæ ö
U è U ø è dø
(3.6.3)
Physically, q is the thickness of a ßuid layer, having velocity U, for which the momentum ßux is the
same as the deÞcit in momentum ßux within the boundary layer (momentum ßux is momentum per unit
time passing a cross section).
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Section 3
Because d* and q are deÞned in terms of integrals for which the integrand vanishes in the freestream,
they are easier to evaluate experimentally than disturbance thickness d.
Exact Solution of the Laminar Flat-Plate Boundary Layer
Blasius obtained an exact solution for laminar boundary layer ßow on a ßat plate. He assumed a thin
boundary layer to simplify the streamwise momentum equation. He also assumed similar velocity proÞles
in the boundary layer, so that when written as u/U = f(y/d), velocity proÞles do not vary with x. He used
a similarity variable to reduce the partial differential equations of motion and continuity to a single thirdorder ordinary differential equation.
Blasius used numerical methods to solve the ordinary differential equation. Unfortunately, the velocity
proÞle must be expressed in tabular form. The principal results of the Blasius solution may be expressed as
d
=
x
5
Re x
(3.6.4)
and
Cf =
tw
0.664
=
1
Re x
rU 2
2
(3.6.5)
These results characterize the laminar boundary layer on a ßat plate; they show that laminar boundary
layer thickness varies as x1/2 and wall shear stress varies as 1/x1/2.
Approximate Solutions
The Blasius solution cannot be expressed in closed form and is limited to laminar ßow. Therefore,
approximate methods that give solutions for both laminar and turbulent ßow in closed form are desirable.
One such method is the momentum integral equation (MIE), which may be developed by integrating
the boundary layer equation across the boundary layer or by applying the streamwise momentum equation
to a differential control volume (Fox and McDonald, 1992). The result is the ordinary differential equation
t
æ d*
ö q dU
dq
= w 2 - ç + 2÷
dx rU
è q
ø U dx
(3.6.6)
The Þrst term on the right side of Equation (3.6.6) contains the inßuence of wall shear stress. Since tw
is always positive, it always causes q to increase. The second term on the right side contains the pressure
gradient, which can have either sign. Therefore, the effect of the pressure gradient can be to either
increase or decrease the rate of growth of boundary layer thickness.
Equation (3.6.6) is an ordinary differential equation that can be solved for q as a function of x on a
ßat plate (zero pressure gradient), provided a reasonable shape is assumed for the boundary layer velocity
proÞle and shear stress is expressed in terms of the other variables. Results for laminar and turbulent
ßat-plate boundary layer ßows are discussed below.
Laminar Boundary Layers. A reasonable approximation to the laminar boundary layer velocity proÞle
is to express u as a polynomial in y. The resulting solutions for d and tw have the same dependence on
x as the exact Blasius solution. Numerical results are presented in Table 3.6.1. Comparing the approximate
and exact solutions shows remarkable agreement in view of the approximations used in the analysis.
The trends are predicted correctly and the approximate values are within 10% of the exact values.
Turbulent Boundary Layers. The turbulent velocity proÞle may be expressed well using a power law,
u/U = (y/d)1/n, where n is an integer between 6 and 10 (frequently 7 is chosen). For turbulent ßow it is
© 1999 by CRC Press LLC
3-73
Fluid Mechanics
TABLE 3.6.1 Exact and Approximate Solutions for Laminar Boundary Layer Flow
over a Flat Plate at Zero Incidence
Velocity Distribution
u
æ yö
= f ç ÷ = f ( h)
è dø
U
f (h) = 2h Ð h2
f (h) = 3/2 h Ð 1/2 h3
f (h) = sin (p/2 h)
Exact
q
d
d*
d
2/15
39/280
(4 Ð p)/2p
0.133
1/3
3/8
(p Ð 2)/p
0.344
a=
d
Re x
x
5.48
4.64
4.80
5.00
b = C f Re x
0.730
0.647
0.654
0.664
not possible to express shear stress directly in terms of a simple velocity proÞle; an empirical correlation
is required. Using a pipe ßow data correlation gives
d 0.382
=
x Re1x 5
(3.6.7)
and
Cf =
tw
0.0594
=
1
Re1x 5
rU 2
2
(3.6.8)
These results characterize the turbulent boundary layer on a ßat plate. They show that turbulent boundary
layer thickness varies as x4/5 and wall shear stress varies as 1/x1/5.
Approximate results for laminar and turbulent boundary layers are compared in Table 3.6.2. At a
Reynolds number of 1 million, wall shear stress for the turbulent boundary layer is nearly six times as
large as for the laminar layer. For a turbulent boundary layer, thickness increases Þve times faster with
distance along the surface than for a laminar layer. These approximate results give a physical feel for
relative magnitudes in the two cases.
TABLE 3.6.2 Thickness and Skin Friction CoefÞcient for Laminar and Turbulent Boundary Layers on a Flat
Plate
Reynolds
Number
2E
5E
1E
2E
5E
1E
2E
5E
+
+
+
+
+
+
+
+
05
05
06
06
06
07
07
07
Boundary Layer Thickness/x
Skin Friction CoefÞcient
Turbulent/Laminar Ratio
Laminar BL
Turbulent BL
Laminar BL
Turbulent BL
BL Thickness
Skin Friction
0.0112
0.00707
0.00500
0.00354
0.00224
0.00158
0.00112
0.000707
0.0333
0.0277
0.0241
0.0210
0.0175
0.0152
0.0132
0.0110
0.00148
0.000939
0.000664
0.000470
0.000297
0.000210
0.000148
0.0000939
0.00517
0.00431
0.00375
0.00326
0.00272
0.00236
0.00206
0.00171
2.97
3.92
4.82
5.93
7.81
9.62
11.8
15.6
3.48
4.58
5.64
6.95
9.15
11.3
13.9
18.3
Note: BL = boundary layer.
The MIE cannot be solved in closed form for ßows with nonzero pressure gradients. However, the
role of the pressure gradient can be understood qualitatively by studying the MIE.
Effect of Pressure Gradient
Boundary layer ßow with favorable, zero, and adverse pressure gradients is depicted schematically in
Figure 3.6.3. (Assume a thin boundary layer, so ßow on the lower surface behaves as external ßow on
© 1999 by CRC Press LLC
3-74
Section 3
FIGURE 3.6.3 Boundary layer ßow with presssure gradient (thickness exaggerated for clarity).
a surface, with the pressure gradient impressed on the boundary layer.) The pressure gradient is favorable
when ¶p/¶x < 0, zero when ¶p/¶x = 0, and adverse when ¶p/¶x > 0, as indicated for Regions 1, 2, and 3.
Viscous shear always causes a net retarding force on any ßuid particle within the boundary layer. For
zero pressure gradient, shear forces alone can never bring the particle to rest. (Recall that for laminar
and turbulent boundary layers the shear stress varied as 1/x1/2 and 1/x1/5, respectively; shear stress never
becomes zero for Þnite x.) Since shear stress is given by tw = m ¶u/¶y)y=0, the velocity gradient cannot
be zero. Therefore, ßow cannot separate in a zero pressure gradient; shear stresses alone can never cause
ßow separation.
In the favorable pressure gradient of Region 1, pressure forces tend to maintain the motion of the
particle, so ßow cannot separate. In the adverse pressure gradient of Region 3, pressure forces oppose
the motion of a ßuid particle. An adverse pressure gradient is a necessary condition for ßow separation.
Velocity proÞles for laminar and turbulent boundary layers are shown in Figure 3.6.2. It is easy to
see that the turbulent velocity proÞle has much more momentum than the laminar proÞle. Therefore,
the turbulent velocity proÞle can resist separation in an adverse pressure gradient better than the laminar
proÞle.
The freestream velocity distribution must be known before the MIE can be applied. We obtain a Þrst
approximation by applying potential ßow theory to calculate the ßow Þeld around the object. Much
effort has been devoted to calculation of velocity distributions over objects of known shape (the ÒdirectÓ
problem) and to determination of shapes to produce a desired pressure distribution (the ÒinverseÓ
problem). Detailed discussion of such calculation schemes is beyond the scope of this section; the state
of the art continues to progress rapidly.
Drag
Any object immersed in a viscous ßuid ßow experiences a net force from the shear stresses and pressure
differences caused by the ßuid motion. Drag is the force component parallel to, and lift is the force
component perpendicular to, the ßow direction. Streamlining is the art of shaping a body to reduce ßuid
dynamic drag. Airfoils (hydrofoils) are designed to produce lift in air (water); they are streamlined to
reduce drag and thus to attain high liftÐdrag ratios.
In general, lift and drag cannot be predicted analytically for ßows with separation, but progress
continues on computational ßuid dynamics methods. For many engineering purposes, drag and lift forces
are calculated from experimentally derived coefÞcients, discussed below.
Drag coefÞcient is deÞned as
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3-75
Fluid Mechanics
CD =
FD
1 2
rV A
2
(3.6.9)
where 1/2rV2 is dynamic pressure and A is the area upon which the coefÞcient is based. Common practice
is to base drag coefÞcients on projected frontal area (Fox and McDonald, 1992).
Similitude was treated in Section 3.3. In general, the drag coefÞcient may be expressed as a function
of Reynolds number, Mach number, Froude number, relative roughness, submergence divided by length,
and so forth. In this section we consider neither high-speed ßow nor free-surface effects, so we will
consider only Reynolds number and roughness effects on drag coefÞcient.
Friction Drag
The total friction drag force acting on a plane surface aligned with the ßow direction can be found by
integrating the shear stress distribution along the surface. The drag coefÞcient for this case is deÞned
as friction force divided by dynamic pressure and wetted area in contact with the ßuid. Since shear
stress is a function of Reynolds number, so is drag coefÞcient (see Figure 3.6.4). In Figure 3.6.4, transition
occurs at Rex = 500,000; the dashed line represents the drag coefÞcient at larger Reynolds numbers. A
number of empirical correlations may be used to model the variation in CD shown in Figure 3.6.4
(Schlichting, 1979).
FIGURE 3.6.4 Drag coefÞcient vs. Reynolds number for a smooth ßat plate parallel to the ßow.
Extending the laminar boundary layer line to higher Reynolds numbers shows that it is beneÞcial to
delay transition to the highest possible Reynolds number. Some results are presented in Table 3.6.3; drag
is reduced more than 50% by extending laminar boundary layer ßow to ReL = 106.
Pressure Drag
A thin ßat surface normal to the ßow has no area parallel to the ßow direction. Therefore, there can be
no friction force parallel to the ßow; all drag is caused by pressure forces. Drag coefÞcients for objects
with sharp edges tend to be independent of Reynolds number (for Re > 1000), because the separation
points are Þxed by the geometry of the object. Drag coefÞcients for selected objects are shown in Table
3.6.4.
Rounding the edges that face the ßow reduces drag markedly. Compare the drag coefÞcients for the
hemisphere and C-section shapes facing into and away from the ßow. Also note that the drag coefÞcient
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3-76
Section 3
TABLE 3.6.3 Drag CoefÞcients for Laminar, Turbulent, and Transition Boundary Layers on a Flat Plate
Reynolds
Number
2E
5E
1E
2E
5E
1E
2E
5E
+
+
+
+
+
+
+
+
05
05
06
06
06
07
07
07
Drag CoefÞcient
Laminar BL
0.00297
0.00188
0.00133
0.000939
0.000594
0.000420
0.000297
0.000188
Turbulent BL
0.00615
0.00511
0.00447
0.00394
0.00336
0.00300
0.00269
0.00235
Transition
Laminar/
Transition
% Drag
Reduction
Ñ
0.00189
0.00286
0.00314
0.00304
0.00284
0.00261
0.00232
Ñ
Ñ
0.464
0.300
0.195
0.148
0.114
0.081
Ñ
Ñ
53.6
70.0
80.5
85.2
88.6
9.19
Note: BL = Boundary layer.
TABLE 3.6.4 Drag CoefÞcient Data for Selected Objects (Re > 1000)
Object
Square prism
3
CD(RE* >
~ 10 )
Diagram
b/h = ¥
2.05
b/h = 1
1.05
Disk
1.17
Ring
1.20b
Hemisphere (open end facing ßow)
1.42
Hemisphere (open end facing downstream)
0.38
C-section (open side facing ßow)
2.30
C-section (open side facing downstream)
1.20
a
b
Data from Hoerner, 1965.
Based on ring area.
for a two-dimensional object (long square cylinder) is about twice that for the corresponding threedimensional object (square cylinder with b/h = 1).
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Fluid Mechanics
Friction and Pressure Drag: Bluff Bodies
Both friction and pressure forces contribute to the drag of bluff bodies (see Shapiro, 1960, for a good
discussion of the mechanisms of drag). As an example, consider the drag coefÞcient for a smooth sphere
shown in Figure 3.6.5. Transition from laminar to turbulent ßow in the boundary layers on the forward
portion of the sphere causes a dramatic dip in drag coefÞcient at the critical Reynolds number (ReD »
2 ´ 105). The turbulent boundary layer is better able to resist the adverse pressure gradient on the rear
of the sphere, so separation is delayed and the wake is smaller, causing less pressure drag.
400
100
10
CD
1
0.01
0.06
100
101
102
103
104
105
106
Re = VD
v
FIGURE 3.6.5 Drag coefÞcient vs. Reynolds number for a smooth sphere.
Surface roughness (or freestream disturbances) can reduce the critical Reynolds number. Dimples on
a golf ball cause the boundary layer to become turbulent and, therefore, lower the drag coefÞcient in
the range of speeds encountered in a drive.
Streamlining
Streamlining is adding a faired tail section to reduce the extent of separated ßow on the downstream
portion of an object (at high Reynolds number where pressure forces dominate drag). The adverse
pressure gradient is taken over a longer distance, delaying separation. However, adding a faired tail
increases surface area, causing skin friction drag to increase. Thus, streamlining must be optimized for
each shape.
Front contours are of principal importance in road vehicle design; the angle of the back glass also is
important (in most cases the entire rear end cannot be made long enough to control separation and reduce
drag signiÞcantly).
Lift
Lift coefÞcient is deÞned as
CL =
FL
1 2
rV A
2
Note that lift coefÞcient is based on projected planform area.
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(3.6.10)
3-78
Section 3
Airfoils
Airfoils are shaped to produce lift efÞciently by accelerating ßow over the upper surface to produce a
low-pressure region. Because the ßow must again decelerate, inevitably there must be a region of adverse
pressure gradient near the rear of the upper surface (pressure distributions are shown clearly in Hazen,
1965).
Lift and drag coefÞcients for airfoil sections depend on Reynolds number and angle of attack between
the chord line and the undisturbed ßow direction. The chord line is the straight line joining the leading
and trailing edges of the airfoil (Abbott and von Doenhoff, 1959).
As the angle of attack is increased, the minimum pressure point moves forward on the upper surface
and the minimum pressure becomes lower. This increases the adverse pressure gradient. At some angle
of attack, the adverse pressure gradient is strong enough to cause the boundary layer to separate
completely from the upper surface, causing the airfoil to stall. The separated ßow alters the pressure
distribution, reducing lift sharply.
Increasing the angle of attack also causes the the drag coefÞcient to increase. At some angle of attack
below stall the ratio of lift to drag, the liftÐdrag ratio, reaches a maximum value.
Drag Due to Lift
For wings (airfoils of Þnite span), lift and drag also are functions of aspect ratio. Lift is reduced and
drag increased compared with inÞnite span, because end effects cause the lift vector to rotate rearward.
For a given geometric angle of attack, this reduces effective angle of attack, reducing lift. The additional
component of lift acting in the ßow direction increases drag; the increase in drag due to lift is called
induced drag.
The effective aspect ratio includes the effect of planform shape. When written in terms of effective
aspect ratio, the drag of a Þnite-span wing is
C D = C D, ¥ +
CL2
par
(3.6.11)
where ar is effective aspect ratio and the subscript ¥ refers to the inÞnite section drag coefÞcient at CL.
For further details consult the references.
The lift coefÞcient must increase to support aircraft weight as speed is reduced. Therefore, induced
drag can increase rapidly at low ßight speeds. For this reason, minimum allowable ßight speeds for
commercial aircraft are closely controlled by the FAA.
Boundary Layer Control
The major part of the drag on an airfoil or wing is caused by skin friction. Therefore, it is important to
maintain laminar ßow in the boundary layers as far aft as possible; laminar ßow sections are designed
to do this. It also is important to prevent ßow separation and to achieve high lift to reduce takeoff and
landing speeds. These topics fall under the general heading of boundary layer control.
Profile Shaping
Boundary layer transition on a conventional airfoil section occurs almost immediately after the minimum
pressure at about 25% chord aft the leading edge. Transition can be delayed by shaping the proÞle to
maintain a favorable pressure gradient over more of its length. The U.S. National Advisory Committee
for Aeronautics (NACA) developed several series of proÞles that delayed transition to 60 or 65% of
chord, reducing drag coefÞcients (in the design range) 60% compared with conventional sections of the
same thickness ratio (Abbott and von Doenhoff, 1959).
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Fluid Mechanics
3-79
Flaps and Slats
Flaps are movable sections near the trailing edge of a wing. They extend and/or deßect to increase wing
area and/or increase wing camber (curvature), to provide higher lift than the clean wing. Many aircraft
also are Þtted with leading edge slats which open to expose a slot from the pressure side of the wing
to the upper surface. The open slat increases the effective radius of the leading edge, improving maximum
lift coefÞcient. The slot allows energized air from the pressure surface to ßow into the low-pressure
region atop the wing, energizing the boundary layers and delaying separation and stall.
Suction and Blowing
Suction removes low-energy ßuid from the boundary layer, reducing the tendency for early separation.
Blowing via high-speed jets directed along the surface reenergizes low-speed boundary layer ßuid. The
objective of both approaches is to delay separation, thus increasing the maximum lift coefÞcient the
wing can achieve. Powered systems add weight and complexity; they also require bleed air from the
engine compressor, reducing thrust or power output.
Moving Surfaces
Many schemes have been proposed to utilize moving surfaces for boundary layer control. Motion in the
direction of ßow reduces skin friction, and thus the tendency to separate; motion against the ßow has
the opposite effect. The aerodynamic behavior of sports balls Ñ baseballs, golf balls, and tennis balls
Ñ depends signiÞcantly on aerodynamic side force (lift, down force, or side force) produced by spin.
These effects are discussed at length in Fox and McDonald (1992) and its references.
Computation vs. Experiment
Experiments cannot yet be replaced completely by analysis. Progress in modeling, numerical techniques,
and computer power continues to be made, but the role of the experimentalist likely will remain important
for the foreseeable future.
Computational Fluid Dynamics (CFD)
Computation of ßuid ßow requires accurate mathematical modeling of ßow physics and accurate numerical procedures to solve the equations. The basic equations for laminar boundary layer ßow are well
known. For turbulent boundary layers generally it is not possible to resolve the solution space into
sufÞciently small cells to allow direct numerical simulation. Instead, empirical models for the turbulent
stresses must be used. Advances in computer memory storage capacity and speed (e.g., through use of
massively parallel processing) continue to increase the resolution that can be achieved.
A second source of error in CFD work results from the numerical procedures required to solve the
equations. Even if the equations are exact, approximations must be made to discretize and solve them
using Þnite-difference or Þnite-volume methods. Whichever is chosen, the solver must guard against
introducing numerical instability, round-off errors, and numerical diffusion (Hoffman, 1992).
Role of the Wind Tunnel
Traditionally, wind tunnel experiments have been conducted to verify the design and performance of
components and complete aircraft. Design veriÞcation of a modern aircraft may require expensive scale
models, several thousand hours of wind tunnel time at many thousands of dollars an hour, and additional
full-scale ßight testing.
New wind tunnel facilities continue to be built and old ones refurbished. This indicates a need for
continued experimental work in developing and optimizing aircraft conÞgurations.
Many experiments are designed to produce baseline data to validate computer codes. Such systematic
experimental data can help to identify the strengths and weaknesses of computational methods.
CFD tends to become only indicative of trends when massive zones of ßow separation are present.
Takeoff and landing conÞgurations of conventional aircraft, with landing gear, high-lift devices, and
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3-80
Section 3
ßaps extended, tend to need Þnal experimental conÞrmation and optimization. Many studies of vertical
takeoff and vectored thrust aircraft require testing in wind tunnels.
Defining Terms
Boundary layer: Thin layer of ßuid adjacent to a surface where viscous effects are important; viscous
effects are negligible outside the boundary layer.
Drag coefÞcient: Force in the ßow direction exerted on an object by the ßuid ßowing around it, divided
by dynamic pressure and area.
Lift coefÞcient: Force perpendicular to the ßow direction exerted on an object by the ßuid ßowing
around it, divided by dynamic pressure and area.
Pressure gradient: Variation in pressure along the surface of an object. For a favorable pressure gradient,
pressure decreases in the ßow direction; for an adverse pressure gradient, pressure increases in
the ßow direction.
Separation: Phenomenon that occurs when ßuid layers adjacent to a solid surface are brought to rest
and boundary layers depart from the surface contour, forming a low-pressure wake region. Separation can occur only in an adverse pressure gradient.
Transition: Change from laminar to turbulent ßow within the boundary layer. The location depends on
distance over which the boundary layer has developed, pressure gradient, surface roughness,
freestream disturbances, and heat transfer.
References
Abbott, I.H. and von Doenhoff, A.E. 1959. Theory of Wing Sections, Including a Summary of Airfoil
Data. Dover, New York.
Fox, R.W. and McDonald, A.T. 1992. Introduction to Fluid Mechanics, 4th ed. John Wiley & Sons, New
York.
Hazen, D.C. 1965. Boundary Layer Control, Þlm developed by the National Committee for Fluid
Mechanics Films (NCFMF) and available on videotape from Encyclopaedia Britannica Educational
Corporation, Chicago.
Hoerner, S.F. 1965. Fluid-Dynamic Drag, 2nd ed. Published by the author, Midland Park, NJ.
Hoffman, J.D. 1992. Numerical Methods for Engineers and Scientists. McGraw-Hill, New York.
Schlichting, H. 1979. Boundary-Layer Theory, 7th ed. McGraw-Hill, New York.
Shapiro, A.H. 1960. The Fluid Dynamics of Drag, Þlm developed by the National Committee for Fluid
Mechanics Film (NCFMF) and available on videotape from Encyclopaedia Britannica Educational
Corporation, Chicago.
Further Information
A comprehensive source of basic information is the Handbook of Fluid Dynamics, edited by Victor L.
Streeter (McGraw-Hill, New York, 1960).
Timely reviews of important topics are published in the Annual Review of Fluid Mechanics series (Annual
Reviews, Inc., Palo Alto, CA.). Each volume contains a cumulative index.
ASME (American Society of Mechanical Engineers, New York, NY) publishes the Journal of Fluids
Engineering quarterly. JFE contains ßuid machinery and other engineering applications of ßuid
mechanics.
The monthly AIAA Journal and bimonthly Journal of Aircraft (American Institute for Aeronautics and
Astronautics, New York) treat aerospace applications of ßuid mechanics.
© 1999 by CRC Press LLC