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The American Society of Mechanical Engineers

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42 TRANSACTIONS OF T H E A.S.M.E. JANUARY, 1941<br />

sions <strong>of</strong> a velocity times a length, and a good physical interpretation<br />

<strong>of</strong> e is given by Bakhmeteff ( l).2 In fully developed<br />

turbulent flow, except near a smooth boundary, the coefficient<br />

pe is many times greater than thus the first term in Equation<br />

[4] becomes quite small compared to the second term.<br />

<strong>The</strong> rate a t which potential or pressure energy is used in producing<br />

flow is equal to r(dU/dy) in foot-pounds per unit volume<br />

<strong>of</strong> fluid. For viscous flow this becomes ti{dU/dy)2, and represents<br />

the rate a t which the energy producing flow is dissipated<br />

into heat a t any point in a fluid. In fully developed turbulent<br />

flow, since the mean shear stress is not influenced by viscosity,<br />

the quantity r(dU/dy) represents the rate at which the pressureenergy<br />

producing flow is transformed into turbulence energy.<br />

<strong>The</strong> turbulence energy is then dissipated into heat by the action<br />

<strong>of</strong> viscosity on the small eddies. However, energy <strong>of</strong> turbulence<br />

is not necessarily dissipated a t the point where it is created;<br />

it can and is diffused by the mixing action <strong>of</strong> the turbulence.<br />

For instance in a uniform conduit, the term r(dU/dy) is greatest<br />

near the boundaries and is zero at the center. <strong>The</strong> energy <strong>of</strong><br />

turbulence produced a t the boundaries is in p art diffused to the<br />

center <strong>of</strong> the conduit and dissipated there. Of course it should<br />

be remembered that, in nonchanging uniform flow, the total rate<br />

a t which energy <strong>of</strong> turbulence is created is equal to the rate <strong>of</strong><br />

dissipation <strong>of</strong> this energy by the action <strong>of</strong> viscosity.<br />

Lamb (5) shows th a t the general equation for the rate <strong>of</strong> dissipation<br />

<strong>of</strong> energy per unit volume in a viscous fluid is<br />

In isotropic turbulence U, V, and IF can be replaced by u, v,<br />

and w. Taylor simplifies Equation [5] by demonstrating the<br />

interrelationship existing between the various mean squares<br />

and mean products <strong>of</strong> the velocity gradients, and obtains<br />

E n e r g y C o n s i d e r a t i o n s f o r I s o t r o p i c T u r b u l e n c e<br />

Because <strong>of</strong> the complexity <strong>of</strong> the turbulence mechanism, any<br />

theoretical considerations m ust start w ith the simplest conditions.<br />

One <strong>of</strong> the types <strong>of</strong> turbulence th a t has received extensive<br />

consideration by physicists interested in wind-tunnel turbulence<br />

phenomena is th a t referred to as isotropic turbulence.<br />

This type <strong>of</strong> turbulence is such th a t (a) the mean values <strong>of</strong><br />

squares and products <strong>of</strong> the fluctuating velocity components,<br />

such as v2 and uv, and their derivatives, such<br />

/d»v<br />

W and<br />

/ dv du\<br />

are independent <strong>of</strong> the location <strong>of</strong> the point observed,<br />

\cto by)<br />

and (b) the same mean values are obtained if the axes <strong>of</strong> reference<br />

are rotated or reflected. Fluids having isotropic turbulence<br />

can have no mean shear or mean-pressure gradient, th a t is,<br />

dU/dy = 0, dU/dx — 0, etc.<br />

In practical hydraulics, isotropic turbulence is hardly ever<br />

attained; however, it is sometimes approached. <strong>The</strong> turbulence<br />

in the center <strong>of</strong> closed conduits is nearly isotropic; also, the<br />

turbulence formed downstream from various turbulence-producing<br />

devices such as screens, grids, expansions, and flow-control<br />

apparatus tends to approach isotropy a t times. As G. I. Taylor<br />

remarks, “there is a strong tendency to isotropy in turbulent<br />

motion.” A study <strong>of</strong> the energy dissipation characteristics <strong>of</strong><br />

isotropic turbulence may throw considerable light on the more<br />

complicated turbulence obtained in many practical hydraulics<br />

problems.<br />

<strong>The</strong> intensity <strong>of</strong> turbulence is usually designated by the ratios<br />

"v/w2/ U, y/v2/U, and "v/w2/ U, and for isotropic turbulence<br />

these are all equal. Investigations by Dryden (2) and others reveal<br />

th at these ratios a t any point beyond any particular turbulence-producing<br />

device tend to be independent<strong>of</strong> the mean velocity.<br />

This relationship also appears to hold for nonisotropic turbulence<br />

a t high Reynolds numbers. <strong>The</strong> decrease in the intensity <strong>of</strong><br />

the turbulence beyond screens and grids in wind tunnels, or<br />

the decay <strong>of</strong> the turbulence, has been studied quite extensively<br />

both theoretically and experimentally by Taylor (3), von K&rm&n<br />

(4), and Dryden (2).<br />

2 Numbers in parentheses refer to the Bibliography at the end <strong>of</strong><br />

the paper.<br />

where X is a length proportional to the small eddies present since<br />

they are primarily responsible for the dissipation <strong>of</strong> the turbulence<br />

energy. Possible methods <strong>of</strong> experimentally determining<br />

v2 and X were discussed by the author in a previous paper (6).<br />

<strong>The</strong> mechanism by which the small eddies are produced from<br />

the larger ones is a fundam ental problem <strong>of</strong> turbulence about<br />

which little is known. I t is these small eddies, referred to sometimes<br />

as the microturbulence, which are largely responsible for<br />

the high rate <strong>of</strong> energy dissipation associated with turbulent<br />

flow.<br />

<strong>The</strong> scale <strong>of</strong> the turbulence, L, which is im portant in regard<br />

to the diffusive action <strong>of</strong> the turbulence, is proportional to the<br />

average size <strong>of</strong> the eddies. <strong>The</strong> product \ / v2L is proportional<br />

to the transverse diffusion coefficient e, as used in Equation [4],<br />

As the turbulence created by some obstruction in a fluid stream<br />

is dissipated downstream, a change in the length factors X and<br />

L takes place which is a characteristic phenomenon <strong>of</strong> decaying<br />

turbulence. Qualitative visual observations <strong>of</strong> the turbulence<br />

in w ater streams beyond grids, throttled valves, sudden expansions,<br />

etc., seem to indicate th a t the average size <strong>of</strong> the eddies<br />

tends to increase as the turbulence is dissipated.<br />

<strong>The</strong> internal stresses in turbulent flow are proportional to the<br />

product <strong>of</strong> the density and the mean square <strong>of</strong> the fluctuating<br />

velocities such as pu1. Any such force will then dissipate energy<br />

at a rate proportional to the product <strong>of</strong> the force and the associated<br />

velocity, thus, p(tt')3, where u' = \ / w 2. <strong>The</strong> total area<br />

on which these forces act will be proportional to the square <strong>of</strong><br />

the scale <strong>of</strong> the eddy system, or to L2, and the rate <strong>of</strong> dissipap<br />

M 3<br />

tion per unit volume will then be proportional to For<br />

isotropic turbulence, this quantity should then be proportional<br />

to the rate <strong>of</strong> energy dissipation given by Equation [6]. <strong>The</strong><br />

following pronortionalitv can then he writ,ten<br />

<strong>The</strong> terms under the radical in Equation [8] have been referred

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