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Figure 1.1. At least 20 30 antennas protrude from the skin of a modern aircraft. (From [Hopkins et al. 1997], reprinted by permission of the American Institute of Aeronautics and Astronautics, Inc.)

If you re migrating an application from Flex 3 to Flex 4, just change the initial character of StyleManager from uppercase to lowercase and the code will work exactly as before. n

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For a standard PBT the error is on the order of 5% if the perpendicular distance is used For the large-bladed impeller with a shallower angle, the errors are up to 70%! This D also makes sense when measuring the primary ow with a laser Doppler velocimeter for determination of the ow number (see 6) It is very important in a mixing installation when one has to be concerned with clearances from the tips of the blades.

u ( z )= 0

Where does this leave us We have three ways to estimate the dissipation and the Kolmogorov length scale: The rst requires experimental information for Cu , CL , and A; the second uses the power number and the impeller swept volume to get an estimate of the maximum local dissipation; the third uses the total volume of the tank to get an estimate of the gross average dissipation and introduces a factor of (D/T)3 into the equation More recent detailed studies on the Rushton turbine in particular (Michelet, 1998; Escudier, 2001) have shown that these estimates are reasonably accurate over some portion of the impeller discharge stream All three methods will allow us to assess trends on scale-up, where physical properties often remain constant, but dimensions and rotational speeds change The power per impeller swept volume is recommended as the best practice estimate Example 2-4a: Blend Time.

Now that we have ways to estimate and the characteristic length scale Ls , we return to Corrsin s equations in Table 2-4 Probably the most important practical point is that the time constant of mixing scales with (L2 / )1/3 All the rest of the terms in the equation for (Sc 1) are either cons stants or relatively minor effects of the Schmidt number For mixing in a pipe, we take the radius of the feed pipe, r0 , as the initial integral length scale, and the uctuating velocity, u, as a measure of the turbulent energy Thus we can write u3 r0 L2 s.

Figure 9.8. Specify scale factor or [Copy/Reference] <0.400>: .4

The application window in Windows (see Figure 10.2) has its own discrete borders, title bar, and controls, including the Application menus incorporated into the band immediately below the application window title bar.

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