The American Society of Mechanical Engineers
The American Society of Mechanical Engineers
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