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The model suggests that in the order of 85 per cent of the injected raw meal has undergone the calcination reaction fully before exit from the precalciner No measurement on the real installation has yet been performed that can verify this The post-processing available shows the discrete phase devolatilization rate per cell from the coal and the raw meal in one field variable This includes the volatiles (lv-vol) from the coal and the CO2 from the raw meal, which is modelled as a volatile despite the true nature of the reaction The model suggests that calcination occurs mainly toward the wall at the right hand side of the precalciner, ie on the side furthest from the TAD above the conical section Since calcination is a highly endothermic reaction, an associated region of relatively low temperature would be consistent with a high rate of calcination.

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This is what is observed in the model; the region corresponding to high calcination rate in the foregoing discussion shows a depression to the range 900 C to 1000 C Energy supplied by the coal combustion reactions maintains the temperature until the calcination reaction is complete The behaviour of the coal in the model is consistent with the above discussion Coal from the inlet on the same side as the Tertiary Air Duct (left-hand side coal inlet) rises and exits without recirculating Coal from the other inlet (right-hand side coal inlet) rises to the ceiling of the precalciner and recirculates in the full length of the main cylindrical section Residence times are 06 to 10 second for coal from the left-hand side and 5 to 18 seconds for coal injected from the right-hand side.

(9.P.1)

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Volatiles are released very quickly due to the high temperature of the gases into which the relatively cold (75 C) coal air stream enters, and the conversion to CO is completed before the exit from the main body of the precalciner Char oxidation is completed before exit from the precalciner for Coal B; 20 per cent of the char from Coal A is not oxidized before exit Some CO is present at the exit from the precalciner at 046 ppm, confirming the presence of reacting char Tyre chips fall and then recirculate similar to the left-hand side injected coal Residence time in the precalciner is sustained by the recirculation 822 Validation data from the vessel, Six access ports are present on the cylindrical section of the precalciner Three are equally spaced on the circumference at two heights (Fig 81); 0.

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6 m above the conical section (elevation 114 m on the model) and 5 m below the top (elevation 204 m) The data from the model at these two heights is presented in Fig 83 Contours of velocity in the vertical, z direction (m/s), temperature ( C), and particle concentration (kg/m3) were related to measurements made on the precalciner Probes were inserted approximately 03 m into the flow from the edge of the refractory lining through the access ports All temperature measurements show good correlation to within 60 C..

tinuous, as in Figure 4.7(a). The kinks caused by fractions of the number of cycles are shown in Figure 4.7(b) and these increase the sidelobe level in the spectrum in Figure 4.7(c) and 4.7(d). The sidelobe level for 6 Hz is the minimum line in Figure 4.7(d).

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In this section, scalar and vector complex stochastic variables are introduced and their most important properties are discussed. Next, the same properties of vectors of both real and complex stochastic variables are addressed.

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true when the input signal becomes large, and distortion and intermodulation arise; this is also the factor determining the upper limit of the dynamic range of the mixer. We will see this case in more detail in the following (Section 7.4). At low levels, noise determines the lower limit of the dynamic range. For a correct evaluation of the noise level in a mixer, the nonlinear behaviour must be taken into account: this will be done in more detail in Section 7.5.

(5.12)

dV _ 4 2 da dt - 1ra dt'

Manipulating ASTs is not for the faint of heart they are low-level beasts that may vary from one release of Python to the next.

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