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364 Chapter 7 ■ Dimensional Analysis, Similitude, and Modeling<br />

It is clear from Eq. 7.19 that geometric similarity<br />

For flow around<br />

bodies, drag is often<br />

the dependent<br />

variable of interest.<br />

as well as Reynolds number similarity<br />

must be maintained. If these conditions are met, then<br />

or<br />

/ im<br />

/ i<br />

/ m /<br />

r m V m / m<br />

m m<br />

e m<br />

/ m<br />

e /<br />

rV/<br />

m<br />

d m<br />

d<br />

1<br />

2rV 2 / 2 1<br />

2r m V 2 2<br />

m / m<br />

d r a V 2<br />

b a / 2<br />

b d<br />

r m V m / m<br />

m<br />

Measurements of model drag, d m , can then be used to predict the corresponding drag, d, on the<br />

prototype from this relationship.<br />

As was discussed in the previous section, one of the common difficulties with models is related<br />

to the Reynolds number similarity requirement which establishes the model velocity as<br />

or<br />

V m m m<br />

m<br />

V m n m<br />

n<br />

r<br />

r m<br />

/<br />

/ m<br />

V<br />

/<br />

/ m<br />

V<br />

(7.20)<br />

(7.21)<br />

where n m n is the ratio of kinematic viscosities. If the same <strong>fluid</strong> is used for model and prototype<br />

so that n m n, then<br />

V m / / m<br />

V<br />

V7.14 Model airplane<br />

test in water<br />

V7.15 Large scale<br />

wind tunnel<br />

and, therefore, the required model velocity will be higher than the prototype velocity for // m<br />

greater than 1. Since this ratio is often relatively large, the required value of V m may be large. For<br />

1<br />

example, for a 10 length scale, and a prototype velocity of 50 mph, the required model velocity is<br />

500 mph. This is a value that is unreasonably high to achieve with liquids, and for gas flows this<br />

would be in the range where compressibility would be important in the model 1but not in the<br />

prototype2.<br />

As an alternative, we see from Eq. 7.21 that V m could be reduced by using a different <strong>fluid</strong><br />

in the model such that n m n 6 1. For example, the ratio of the kinematic viscosity of water to that<br />

1<br />

of air is approximately 10, so that if the prototype <strong>fluid</strong> were air, tests might be run on the model<br />

using water. This would reduce the required model velocity, but it still may be difficult to achieve<br />

the necessary velocity in a suitable test facility, such as a water tunnel.<br />

Another possibility for wind tunnel tests would be to increase the air pressure in the tunnel<br />

so that r m 7 r, thus reducing the required model velocity as specified by Eq. 7.20. Fluid viscosity<br />

is not strongly influenced by pressure. Although pressurized tunnels have been used, they are<br />

obviously more complicated and expensive.<br />

The required model velocity can also be reduced if the length scale is modest; that is, the<br />

model is relatively large. For wind tunnel testing, this requires a large test section which greatly<br />

increases the cost of the facility. However, large wind tunnels suitable for testing very large models<br />

1or prototypes2 are in use. One such tunnel, located at the NASA Ames Research Center, Moffett<br />

Field, California, has a test section that is 40 ft by 80 ft and can accommodate test speeds to<br />

345 mph. Such a large and expensive test facility is obviously not feasible for university or industrial<br />

laboratories, so most model testing has to be accomplished with relatively small models.

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