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Thixoforming : Semi-solid Metal Processing

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184j 6 Modelling the Flow Behaviour of <strong>Semi</strong>-<strong>solid</strong> <strong>Metal</strong> Alloys<br />

Figure 6.16 Equilibrium viscosity curves for different <strong>solid</strong> fractions. Material: X210CrW12.<br />

become apparent. The agglomeration state is assumed to remain constant momentarily<br />

if the shear rate is suddenly changed from a basis shear rate to a higher or lower<br />

one. As a result, Newtonian flow behaviour is anticipated, but, as already observed for<br />

tin–lead [12, 27] and aluminium alloys [13, 22]. So far, this phenomenon cannot be<br />

explained. In the model approach (Equation 6.3) the flow exponent m describes the<br />

isostructural behaviour when k remains constant.<br />

Figure 6.16 shows the steady-state flow curves generated from Figure 6.14.<br />

Figure 6.17 more clearly displays the flow curve for the liquid material ( fs ¼ 0%),<br />

which shows as expected Newtonian properties with a viscosity of 50 mPa s. The<br />

high fluctuations in the liquid measurements result from the bearing of the rod as the<br />

momentum of the bearing is in the range of that from the liquid metal.<br />

The shear rate jump experiments are used to calculate initial model parameters<br />

from Equation 6.3, which in turn can be utilized for the more exact inverse parameter<br />

determination described in Section 6.2.4.2. Figure 6.18 exemplarily shows a comparison<br />

between experimental data and the modelling approach for a <strong>solid</strong> fraction of<br />

33%. The model is able to predict the flow behaviour in a reasonable range. The main<br />

disagreement is observed for the jump downwards immediately after material<br />

preparation. This phenomenon can be discerned also for aluminium or tin–lead<br />

alloys but cannot be explained at the moment.<br />

Figure 6.17 Flow curve for liquid X210CrW12.

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