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Those of you running a very basic setup will want to be able to play audio clips and maybe even background music. I do this today on my Windows machine with Winamp (http:// winamp.com) and on my Mac Mini with QuickTime (http://apple.com). QuickTime is versatile in that I can open up more than one instance of the program on my desktop to create a queuing system. Figure 8-9 shows multiple instances of QuickTime and Winamp loaded on my desktop. So, what happens is this: While I am recording my show, I keep these windows open so that I can play my intro, which is queued, and when needed, I can play a couple of segment fillers. Here is my typical setup: 1. I have my show set up in a play list, so I load Winamp and load the play list with the intro. I play the clip and make sure that the audio will not be about the same level as my voice. 2. If I have received promotional clips or have an advertiser spot, I load those in QuickTime, as I can very quickly open multiple instances of QuickTime by selecting New Player in the QuickTime menu. 3. I then make sure that Audacity has Stereo or What U Hear selected prior to starting the show. 4. When I m ready, I can start Audacity recording and play the intro to start the show. As I progress in my show notes, I then play the audio clips I have loaded in QuickTime.



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Figure 8.2 shows some features of the model precalciner operation. The outline shows the edges of the precalciner vessel, with the exit duct directed away from the point of observation. Velocity vectors are projected from lines across the centre of the vessel at 10 heights. Temperature contours are plotted on two planes, at 11.4 m, and at 20.4 m from the base. These are at the height of available access ports in the wall of the real precalciner, which will be referred to in the validation section. The behaviour of the particles in the model are represented by three coal particle trajectories from each of the coal inlets and six tyre chip trajectories from the tyre inlet. Some qualitative aspects of the predicted behaviour will be drawn from this figure in the following sections. 8.2.1 CFD results The model shows that particles injected at the raw meal inlet (RMI), are strongly influenced by the gases injected at the tertiary air duct (TAD). Of the mass of raw meal injected approximately 85 per cent is driven across to the far side. The momentum of the gases from the TAD is 27 kg/s at 30 m/s compared to 55 kg/s of raw meal particles at approximately 15 m/s. The effect of turbulence in the real installation tends to disperse the particles in random patterns. CFD shows that the initial common trajectory is toward the right-hand side of the precalciner in the conical section, despite turbulence effects. The effect of turbulence is significant in dispersing the particles following their passage beyond the throat of the conical section. There is then significant recirculation of some particles in the main cylindrical section before exit. The time a particle will take to traverse from inlet to exit thus varies considerably;

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Of course, to employ (10.88) will generally involve solving a nonlinear system of equations for xn+1 and yn+1 , necessitating the use of 7 techniques. As before, we refer to parameter h as the step size. The accuracy of the explicit and implicit Euler methods for systems is the same as for individual equations; speci cally, it is O(h2 ). However, stability analysis is more involved. Matrix methods simply cannot be avoided. This is demonstrated as follows. The model problem for a single rst-order ODE was Eq. (10.28). For a coupled system of two rst-order ODEs as in (10.85), the model problem is now dx = a00 x + a01 y, dt dy = a10 x + a11 y. dt (10.89a) (10.89b)

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Addition p(x) + q(x) has the characteristic function C(n) + D(n) Multiplication by a constant a p(x) has the characteristic function aC(n) Scaling 1 n C p(a x) has the characteristic function jaj a

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