lab-x
Laboratory Report 4 Wind Tunnel
Prepared by: Group 4
Cooper Auge John Bergum Alex Franke Ryan Kunz Gage Wavra
Prepared for:
Dr. Vida Atashi
University of North Dakota Civil Engineering Department CE 423 Civil Engineering Hydraulic Engineering Laboratory – Spring 2024
Lab Completed: 02/06/2024
Date Submitted: 02/13/2024
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Table of Contents
1. Introduction........................................................................................................................................1
2. Objectives...........................................................................................................................................2
3. Experimental Design...........................................................................................................................2
4. Relevant Equations.............................................................................................................................3
5. Equipment and Materials....................................................................................................................5
6. Procedures..........................................................................................................................................5
7. Results................................................................................................................................................5
8. Discussion and Conclusions..............................................................................................................13
9. References........................................................................................................................................13
10. Appendices...................................................................................................................................14
10.1 Appendix A....................................................................................................................................14
10.2 Appendix B.....................................................................................................................................16
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List of Tables
Table 1 Test Data for 113 ft/s Flow.............................................................................................................7
Table 2 Test Data for 102 ft/s Flow.............................................................................................................9
Table 3 Test Data for 98 ft/s Flow.............................................................................................................11
Table 4 Experimental Results Summary for Each Tested Flow Velocity..................................................13
List of Figures
Figure 1 Experimental Design Diagram........................................................................................................3
Figure 2 Static Pressure vs Angular Position for 113 ft/s Flow...................................................................8
Figure 3 Static Pressure vs Angular Position for 102 ft/s Flow.................................................................10
Figure 4 Static Pressure vs Angular Position for 98 ft/s Flow...................................................................12
Figure 5 Schematic for Angular Positions on Cylinder...............................................................................16
Figure 6 Published Values for the Drag Coefficient....................................................................................16
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1. Introduction
Air flow with varying Reynolds numbers (Re) around a circular cylinder in a wind tunnel
produces distinct effects on the calculation of their corresponding drag coefficients (Cd).
Reynolds number represents the ratio of inertial forces to viscous forces and is crucial in
determining flow state characteristics. “…the drag force on the static cylinder increases, reaches
a maximum value, decreases, and stabilizes” (P.V.S. Souza, 2017). At low Reynolds numbers,
the flow around the cylinder is laminar, characterized by smooth and orderly layers of air. In this
state, the drag coefficient tends to be relatively low and stable. However, as Reynolds number
increases, the flow transitions into a turbulent state, marked by chaotic and irregular motion of
air particles. In the turbulent state, the drag coefficient typically increases due to the intensified
mixing and separation of airflow around the cylinder.
In wind tunnel experiments, observing the effects of Reynolds numbers on drag coefficients
helps engineers and researchers understand aerodynamic behavior under different flow
conditions. “The drag coefficient expresses the ratio of the drag force to the force produced by
the dynamic pressure times the area. In a controlled environment (wind tunnel) the velocity,
density, and area can be set so the drag force can be measured. Through division we arrive at a
value for the drag coefficient” (Wind Tunnel- Force, 2015). Low Reynolds numbers often result
in predictable and steady flow patterns, enabling accurate predictions of drag coefficients. As
Reynolds numbers increase, the transition to turbulent flow introduces complexities such as
increased drag, vortex shedding, and separation regions, leading to higher drag coefficients. By
systematically varying Reynolds numbers in wind tunnel experiments, scientists can map out the
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aerodynamic characteristics of the cylinder across different flow regimes, providing valuable
insights for designing efficient structures and vehicles.
Additionally, the point of highest pressure is located at the stagnation point. Generally, the
leading edge of the shape where flow velocity is zero is the point at which the stagnation point
occurs (Dockter, 2024). Velocity head is minimized to zero. The net pressure can be added up to
calculate the net pressure change on the object in the cylinder.
2. Objectives
The objective of this lab was to examine the effects of air flow with different Reynolds
numbers (Re) around a circular cylinder in a wind tunnel with the intention of calculating
their corresponding drag coefficient (C ¿¿d)¿. To do so, the experiment will be performed at
three different air flow rates (v0), and 19 different pressure head (h in inches of H 2O) values
that are measured from tubes connected to the cylinder. The data was captured and computed
into this report, and sample calculations are shown.
3. Experimental Design
The experimental set up consists of a wind tunnel with a test cylinder of known height
and diameter set within the tunnel. A series of 19 manometers is connected to one side of the
cylinder to measure the pressure head (hi) for various points covering 180 ° of the cylinder’s
circumference. At its rear end, the wind tunnel has a series of stacked tubes to attempt to
stimulate laminar flow into the test area. The front (exit) end of the tunnel consists of a large
fan to bring the air up to a certain air flow speed (v0). Having measured the different pressure
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head values, the data can be compiled into a table and static pressure (P-Static), incremental
drag force ¿, and total drag force ¿ can be calculated.
4. Relevant Equations
The static pressure (P or ) can be found by taking the difference of the maximum pressure
head (hmax) and the pressure head (hi∨hx) at various points on the cylinder, and multiplying
it by a conversion factor to convert inches H 2O to lbs
ft2 .
Pi( lbs ft2 )=(hmax−hx)(5.20
lbs
ft3
inches H 2O )
The incremental drag force (∆ Fd) at a selected point can be calculated using the static
pressure at that point (Pi), known height of the cylinder (H=0.875 ft ), known diameter of
the cylinder (D=0.292 ft ), and the angular position (θ) at the selected point.
∆ Fd , i ( lbs )=2π (Pi)(HD)( ∆θ 360 °
)(cos (θ ))
The incremental drag force for each of the 19 points can be added together ¿ to find the total
drag force for half of the cylinder. This value only accounts for half of the total drag force
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Figure 1 Experimental Design Diagram
value because the 19 points of measurement are only located on one side of the cylinder.
Therefore, the total drag force (Fd) can be calculated as such.
Fd ( lbs )=2(∑ ∆ Fd ,i)
Next, the air flow velocity (vo) can be calculated from the max static pressure value (Pmax),
and the density of air (ρair). The air flow velocity will be determined for each of the three
tests to calculate the succeeding values needed for this experiment. Also, the density of air is
found with an equation that includes barometric pressure, a given gas constant for air (R),
and the ambient temperature (T). The calculated density of air is shown in the laboratory
manual for this experiment (ρair=0.00229 slugs
ft3 ¿ .
v0( ft s )=√ 2(Pmax)
ρair
The Reynolds Number (Re) for a selected air flow can be calculated by using the calculated
stream velocity (vo¿, given cylinder diameter (D), calculated density of air (ρair), and the
dynamic viscosity of air (μ) which can be found in the Table of Mechanical Properties of air
at T ambient, the value of which is equal to 3.85 x10−7( lbs × s
ft2 ). The equation is given as
follows.
ℜ= vo D ρair
μair
To calculate the drag coefficient for a certain air flow around the test cylinder, the projected
area ( Ap) must first be calculated. The equation for which is shown below and is based on
the given values of height (H) and diameter (D) of the cylinder.
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Ap ( ft2 )=HD
The drag coefficient (Cd ) equation comes from combining the calculated values of total drag
force (Fd), projected area ( Ap), air flow velocity (vo¿ for each of the three different air speeds.
This calculated value can be compared to the published drag coefficient which can be found by
inspecting the published Wind Tunnel Drag Coefficients chart for a rough cylinder.
Cd= Fd
Ap
ρair vo 2
2
5. Equipment and Materials
Wind tunnel.
Circular cylinder.
Series of nineteen manometers connected to the test cylinder.
6. Procedures
First place the circular cylinder into the wind tunnel before turning it on. You are then to
set a speed at which the fan will run. Then, read the different manometer readings which will
be used to calculate the force on the cylinder. Repeat this with two more additional fan
speeds to complete the data collection portion of this lab.
7. Results
In the following discussions the published drag coefficient is referred to. These published
drag coefficients are the drag coefficients determined by the graph in Appendix B for a rough
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cylinder. These are compared with the calculated drag coefficient throughout this report.
Appendix B also shows a picture explaining the angular positions used throughout the
experiment. The point at which θ=0 is the far-left side of the picture. The first manometer is at
the 5˚ position and increased by 10˚ from there to get the position of the next manometer.
Tables 1, 2, and 3 show the data collected at each of the 19 manometers for the 113 ft/s, 102
ft/s, and 98 ft/s air flows, respectively. Each manometer’s angular position is given for the point
of the cylinder that it represents. The density of air, dynamic viscosity, and Reynolds number for
the flows are shown at the bottom of each table. From these values, the static pressure, drag
force, and cumulative drag force were calculated values and are displayed in each table. This
value is two times the cumulative drag force found because we only analyzed one side of the
cylinder. These were calculated using the equations in part 4 of this report. Finally, the drag
coefficient was determined, this is shown at the bottom of each table.
Figures 1, 2, and 3 show the relationship between static pressure and angular position.
As one can see, the static pressure is 0 where the maximum manometer reading occurred. The
static pressure and the manometer readings are inversely related. When the readings are high on
the manometers, the calculated static pressures are lower. In all the figures the stagnation point
occurs at the smallest angular position (θ=0), this is where the static pressure is maximized.
Table 1 displays the data for the 113 ft/s flow. The highest static pressure found in this trial
was 43.2 and it occurred at cumulative 75˚. The minimum reading, 43.2 occurred at the point
closest to the stagnation point (θ=5˚). This was the highest pressure seen between all the trials
since this flow was the fastest. After all the calculations had been completed, the cumulative
drag force was found to be 1.094lbs. From this, the drag coefficient for the 113 ft/s flow was
determined to be 0.29. This was considerably lower than the published drag coefficient of 0.91.
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Table 1 Test Data for 113 ft/s Flow
Velocit y
(ft/sec)
Pressur e
Sensor
Static Pressur
e (in, H2O)
P-Static (lb/ft2)
Δ Ө (degrees
)
∑Ө (degrees
) Cos ∑Ө Δ Fd (lb) Cumulative
∑Fd (lb)
112.77 hmin 40.4 0 hmax 43.2 14.56 h1 40.4 14.56 5 5 0.9962 0.3234 0.3234 h2 40.5 14.04 10 15 0.9659 0.6048 0.9282 h3 40.8 12.48 10 25 0.9063 0.5044 1.4325 h4 41.2 10.4 10 35 0.8192 0.3799 1.8124 h5 41.6 8.32 10 45 0.7071 0.2623 2.0748 h6 42.3 4.68 10 55 0.5736 0.1197 2.1945 h7 42.9 1.56 10 65 0.4226 0.0294 2.2239 h8 43.2 0 10 75 0.2588 0.0000 2.2239 h9 43.1 0.52 10 85 0.0872 0.0020 2.2259 h10 43.1 0.52 10 95 -0.0872 -0.0020 2.2239 h11 43.1 0.52 10 105 -0.2588 -0.0060 2.2179 h12 42.7 2.6 10 115 -0.4226 -0.0490 2.1689 h13 41.2 10.4 10 125 -0.5736 -0.2660 1.9029 h14 42.3 4.68 10 135 -0.7071 -0.1476 1.7553 h15 42.2 5.2 10 145 -0.8192 -0.1899 1.5654 h16 40.8 12.48 10 155 -0.9063 -0.5044 1.0610 h17 42.3 4.68 10 165 -0.9659 -0.2016 0.8594 h18 42.3 4.68 10 175 -0.9962 -0.2079 0.6515 h19 42.3 4.68 5 180 -1.0000 -0.1043 0.5471
Fd = 1.0943
*ρair = 0.0023 slugs/ft3
*μ = 3.85*10-7 ft2/sec
*Re = (vDρair)/μ *= (112.77*0.292*0.00229)/(3.85*10-7) = 195855 *Cd = Fd/(v2Apρair/2)
= 1.0943/(0.292*0.875*0.00229*112.772/2) 0.29
In Figure 1, the relationship between static pressure and angular position is shown for the
113 ft/s flow. From the figure, it is seen that the minimum static pressure occurred at angular
position 75˚. As one follows the perimeter of the cylinder, static pressure starts high, lowers to
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zero, then experiences two surges in pressures before falling back down again. These peaks seem
absurd, but they also occurred in Figure 2 and Figure 3.
0 20 40 60 80 100 120 140 160 180 0
2
4
6
8
10
12
14
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Velocity = 112.77 ft/s
Angular Position ( ∑Ө )
Pr es
su re
(l b/
ft^ 2)
Figure 2 Static Pressure vs Angular Position for 113 ft/s Flow
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Table 2 displays the data for the 102 ft/s flow. In this trial, the maximum manometer
reading was 42.6 and occurred at angular position 75˚. The minimum reading, 40.9 occurred at
the point closest to the stagnation point (θ=5˚). The cumulative drag force was calculated to be
0.577lbs. From this the value of 0.19 was obtained for the drag coefficient. The slower flow
analyzed in Table 2 resulted in a lower drag coefficient than the one found in the faster flow
analyzed in Table 1. Although the drag coefficient was supposed to be slightly lower for this
lower flow than the 113 ft/s flow, it still was significantly lower than the published value of 0.89.
Table 2 Test Data for 102 ft/s Flow
Velocit y
(ft/sec)
Pressur e
Sensor
Static Pressur
e (in, H2O)
P-Static (lb/ft2)
Δ Ө (degrees
)
∑Ө (degrees
) Cos ∑Ө Δ Fd (lb) Cumulative
∑Fd (lb)
102.20 hmin 40.9 3.12 hmax 42.6 11.96 h1 40.9 11.96 5 5 0.9962 0.2657 0.2657 h2 41 11.44 10 15 0.9659 0.4928 0.7584 h3 41.1 10.92 10 25 0.9063 0.4413 1.1997 h4 41.4 9.36 10 35 0.8192 0.3419 1.5417 h5 41.6 8.32 10 45 0.7071 0.2623 1.8040 h6 42.1 5.72 10 55 0.5736 0.1463 1.9503 h7 42.4 4.16 10 65 0.4226 0.0784 2.0287 h8 42.6 3.12 10 75 0.2588 0.0360 2.0647 h9 42.5 3.64 10 85 0.0872 0.0141 2.0789 h10 42.5 3.64 10 95 -0.0872 -0.0141 2.0647 h11 42.5 3.64 10 105 -0.2588 -0.0420 2.0227 h12 42.3 4.68 10 115 -0.4226 -0.0882 1.9345 h13 41.9 6.76 10 125 -0.5736 -0.1729 1.7616 h14 42 6.24 10 135 -0.7071 -0.1968 1.5648 h15 42 6.24 10 145 -0.8192 -0.2279 1.3369 h16 41.2 10.4 10 155 -0.9063 -0.4203 0.9166 h17 42.1 5.72 10 165 -0.9659 -0.2464 0.6702 h18 42.1 5.72 10 175 -0.9962 -0.2541 0.4161 h19 42.1 5.72 5 180 -1.0000 -0.1275 0.2886
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Fd = 0.5771
*ρair = 0.0023 slugs/ft3
*μ = 3.85*10-7 ft2/sec
*Re = (vDρair)/μ *= (102.2*0.292*0.00229)/(3.85*10-7) = 177504 *Cd = Fd/(v2Apρair/2)
= 0.5771/(0.292*0.875*0.00229*102.22/2) 0.19
Figure 2 shows the relationship between static pressure and angular position for the 102
ft/s flow. This figure looks very similar to Figures 1 and 3 as it should, but there is only 1
distinct peak. The first peak after the static pressure goes to zero is not as clear as it is in Figures
1 and 3.
0 20 40 60 80 100 120 140 160 180 0
2
4
6
8
10
12
14
Velocity = 102.2 ft/s
Angular Position ( ∑Ө )
Pr es
su re
(l b/
ft^ 2)
Figure 3 Static Pressure vs Angular Position for 102 ft/s Flow
Table 3 shows the data for the 98 ft/s flow. In this trial the maximum manometer reading
was 42.4 and occurred at the angular position 75˚. The minimum reading, 41.4 occurred at the
point closest to the stagnation point (θ=5˚). The cumulative drag force was calculated to be
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0.1345. Due to this, the drag coefficient was 0.05, which was much lower than the 113 ft/s and
102 ft/s trials. In all three trials, the drag coefficient was much lower than the published value.
For the 98 ft/s flow this value was supposed to be around 0.80.
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Table 3 Test Data for 98 ft/s Flow
Velocit y
(ft/sec)
Pressur e
Sensor
Static Pressur
e (in, H2O)
P-Static (lb/ft2)
Δ Ө (degrees
)
∑Ө (degrees
) Cos ∑Ө Δ Fd (lb) Cumulative
∑Fd (lb)
97.658 hmin 41.1 4.16 hmax 42.4 10.92 h1 41.1 10.92 5 5 0.9962 0.2426 0.2426 h2 41.2 10.4 10 15 0.9659 0.4480 0.6905 h3 41.3 9.88 10 25 0.9063 0.3993 1.0898 h4 41.5 8.84 10 35 0.8192 0.3229 1.4127 h5 41.7 7.8 10 45 0.7071 0.2460 1.6587 h6 42 6.24 10 55 0.5736 0.1596 1.8183 h7 42.3 4.68 10 65 0.4226 0.0882 1.9065 h8 42.4 4.16 10 75 0.2588 0.0480 1.9545 h9 42.3 4.68 10 85 0.0872 0.0182 1.9727 h10 42.3 4.68 10 95 -0.0872 -0.0182 1.9545 h11 42.3 4.68 10 105 -0.2588 -0.0540 1.9005 h12 42.2 5.2 10 115 -0.4226 -0.0980 1.8025 h13 41.5 8.84 10 125 -0.5736 -0.2261 1.5764 h14 42 6.24 10 135 -0.7071 -0.1968 1.3796 h15 42 6.24 10 145 -0.8192 -0.2279 1.1517 h16 41.3 9.88 10 155 -0.9063 -0.3993 0.7524 h17 42 6.24 10 165 -0.9659 -0.2688 0.4836 h18 42 6.24 10 175 -0.9962 -0.2772 0.2064 h19 42 6.24 5 180 -1.0000 -0.1391 0.0673
Fd = 0.1345
*ρair = 0.0023 slugs/ft3
*μ = 3.85*10-7 ft2/sec
*Re = (vDρair)/μ *= (97.658*0.292*0.00229)/(3.85*10-7) = 169615 *Cd =
Fd/(v2Apρair/2) = 0.1345/
(0.292*0.875*0.00229*97.6582/2) 0.05
Figure 3 shows the relationship between static pressure and angular position for the 98
ft/s flow. This figure looks like Figures 1 and 2, but with lower maximum values and higher
minimum values. The two peaks after static pressure was minimized are distinct, unlike Figure
2. The minimum pressure in Figure 3 was significantly higher than the minimum values in
Figures 1 and 2.
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0 20 40 60 80 100 120 140 160 180 0
2
4
6
8
10
12
Velocity = 97.658 ft/s
Angular Position ( ∑Ө )
Pr es
su re
(l b/
ft^ 2)
Figure 4 Static Pressure vs Angular Position for 98 ft/s Flow
Table 4 compares the calculated drag coefficients with the published drag coefficients
found by the graph in Appendix B. By looking at the table, one can see that with slower flows,
the difference between the calculated and published drag coefficients got much higher. Even
though the published drag coefficients got smaller with slower flows, the calculated drag
coefficients dropped faster so the differences increased. The trend of the calculated values being
significantly lower than the published values must have been due to the head loss through the
tubes making up the manometers.
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Table 4 Experimental Results Summary for Each Tested Flow Velocity
Trial # Velocity
(ft/s) Reynold's Number
Calculated Drag
Coefficien t
Published Drag
Coefficien t
Difference in Drag
Coefficient s
1 112.8 1.959*105 0.29 0.91 68.13%
2 102.2 1.775*105 0.19 0.89 78.65%
3 97.66 1.696*105 0.05 0.80 93.75%
8. Discussion and Conclusions
The objective of this lab was to examine the effects of air flow with different Reynolds
numbers (Re) around a circular cylinder in a wind tunnel with the intention of calculating their
corresponding drag coefficient (C ¿¿d)¿. For the velocity of 113 ft/s the found drag coefficient
was found to be 0.29. This is much less than the expected value of 0.91, leading to a difference
of 68.13%. For a velocity of 102 ft/s the calculated drag coefficient was found to be 0.19. The
expected value is determined to be 0.89. This leads to an error of 78.65%. For the last velocity
of 98 ft/s, the drag coefficient was calculated to be 0.05. This calculation has the most
calculated error, with the expected value to 0.80, the difference between the two is 93.75%. In
conclusion, there seemed to be a lot of error within this lab. Our group compared data with
other groups and their findings were similar, this leads to a conclusion of the experiment having
some reoccurring unknown flaw or head-loss within the manometer tubing.
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9. References
Dockter, B. (2024). Laboratory #4.
P.V.S. Souza, D. G. (2017). Drag force in wind tunnels: A new method. Physica A: Statistical Mechanics and its Applications, 120-128.
Wind Tunnel- Force. (2015). Wind Tunnel Fundamentals.
10. Appendices
10.1 Appendix A.
Sample calculations will be based on Tube # h10 for the first air flow velocity of 112.77 ft/s.
Equation I
P10=( hmax−hx ) (5.20 )= lbs
ft 2
P10=(43.2inches H 2O−43.1inches H 2O )(5.20 lbs
ft2
inches H 2O )=0.52 lbs ft2
Equation II
∆ Fd , 10=2π (P i)(HD )( ∆ θ 360 °
)(cos (θ ))=lbs
∆ Fd10=2 π (0.52 lbs
ft2 )(0.875 ft)(0.292 ft)( 10 ° 360 ° ) (0.08756 )=0.00203 lbs
Equation III
Fd=2 (∑ ∆ Fd ,1−19 )=lbs
15
Fd=2 (0.54714 lbs )=1.0943 lbs
Equation IV
v0=√ 2 ( Pmax ) ρair
= ft s
vo=√ 2(14.56 lbs ft 2
)
0.00229 slug
ft3
=112.7659 ft s
Equation V
ℜ= vo D ρair
μair
=¿
ℜ= (112.7659 ft
s )(0.292 ft )(0.00229 slug
ft3 )
(3.85 x10−7 lbs× s ft2
) =1.9586 x105
Equation VI
Ap ( ft2 )=HD=ft2
Ap=(0.875 ft ) (0.292 ft )=0.2555 ft2
Equation VII
Cd= Fd
Ap
ρair vo 2
2
=¿
16
Cd= 1.0943lbs
(0.2555 ft2) (0.00229 slug
ft3 )(112.7659 ft s )
2
2
=0.29
10.2 Appendix B.
Figure 5 Schematic for Angular Positions on Cylinder
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Figure 6 Published Values for the Drag Coefficient
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