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8.3 Fully Developed Turbulent Flow 401<br />

laminar rather than turbulent. As shown in Chapter 9, turbulence can also aid in delaying flow<br />

separation.<br />

F l u i d s i n t h e N e w s<br />

Smaller heat exchangers Automobile radiators, air conditioners,<br />

and refrigerators contain heat exchangers that transfer energy<br />

from (to) the hot (cold) <strong>fluid</strong> within the heat exchanger<br />

tubes to (from) the colder (hotter) surrounding <strong>fluid</strong>. These<br />

units can be made smaller and more efficient by increasing the<br />

heat transfer rate across the tubes’ surfaces. If the flow through<br />

the tubes is laminar, the heat transfer rate is relatively small.<br />

Significantly larger heat transfer rates are obtained if the flow<br />

within the tubes is turbulent. Even greater heat transfer rates<br />

can be obtained by the use of turbulence promoters, sometimes<br />

termed “turbulators,” which provide additional turbulent mixing<br />

motion than would normally occur. Such enhancement<br />

mechanisms include internal fins, spiral wire or ribbon inserts,<br />

and ribs or grooves on the inner surface of the tube. While these<br />

mechanisms can increase the heat transfer rate by 1.5 to 3 times<br />

over that for a bare tube at the same flowrate, they also increase<br />

the pressure drop (and therefore the power) needed to produce<br />

the flow within the tube. Thus, a compromise involving increased<br />

heat transfer rate and increased power consumption is<br />

often needed.<br />

V8.6 Stirring cream<br />

into coffee<br />

Turbulent flow parameters<br />

can be described<br />

in terms of<br />

mean and fluctuating<br />

portions.<br />

Turbulence is also of importance in the mixing of <strong>fluid</strong>s. Smoke from a stack would continue<br />

for miles as a ribbon of pollutant without rapid dispersion within the surrounding air if the<br />

flow were laminar rather than turbulent. Under certain atmospheric conditions this is observed to<br />

occur. Although there is mixing on a molecular scale 1laminar flow2, it is several orders of magnitude<br />

slower and less effective than the mixing on a macroscopic scale 1turbulent flow2. It is considerably<br />

easier to mix cream into a cup of coffee 1turbulent flow2 than to thoroughly mix two colors<br />

of a viscous paint 1laminar flow2.<br />

In other situations laminar 1rather than turbulent2 flow is desirable. The pressure drop in pipes<br />

1hence, the power requirements for pumping2 can be considerably lower if the flow is laminar rather<br />

than turbulent. Fortunately, the blood flow through a person’s arteries is normally laminar, except<br />

in the largest arteries with high blood flowrates. The aerodynamic drag on an airplane wing can<br />

be considerably smaller with laminar flow past it than with turbulent flow.<br />

8.3.2 Turbulent Shear Stress<br />

The fundamental difference between laminar and turbulent flow lies in the chaotic, random behavior<br />

of the various <strong>fluid</strong> parameters. Such variations occur in the three components of velocity, the<br />

pressure, the shear stress, the temperature, and any other variable that has a field description. Turbulent<br />

flow is characterized by random, three-dimensional vorticity 1i.e., <strong>fluid</strong> particle rotation or<br />

spin; see Section 6.1.32. As is indicated in Fig. 8.12, such flows can be described in terms of their<br />

mean values 1denoted with an overbar2 on which are superimposed the fluctuations 1denoted with<br />

a prime2. Thus, if u u1x, y, z, t2 is the x component of instantaneous velocity, then its time mean<br />

1or time-average2 value, u, is<br />

u 1 T t 0T<br />

(8.24)<br />

where the time interval, T, is considerably longer than the period of the longest fluctuations, but considerably<br />

shorter than any unsteadiness of the average velocity. This is illustrated in Fig. 8.12.<br />

The fluctuating part of the velocity, u¿ , is that time-varying portion that differs from the average<br />

value<br />

u u u¿ or u¿ u u<br />

Clearly, the time average of the fluctuations is zero, since<br />

t 0<br />

u1x, y, z, t2 dt<br />

u¿ 1 T t 0T<br />

1u u 2 dt 1 T a t 0T<br />

t 0 T<br />

u dt u dtb<br />

(8.25)<br />

t 0<br />

t 0<br />

t 0<br />

1 1T u T u2 0<br />

T

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