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Thixoforming : Semi-solid Metal Processing

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load on the temperature-sensitive measurement module is minimized. The whole<br />

spindle of length 550 mm needs to be pivoted to prevent an eccentric or vibrating<br />

rotation. Additionally, the rod is centred in the fixed cup as the tip of the rod<br />

(Figure 6.6) rotates in a small depression in the bottom of the cup. The momentum of<br />

the bearing is predetermined and subtracted from each measurement. Oxidation of<br />

the sample surface is avoided by flushing the void above with preheated argon. The<br />

measuring system was calibrated using silicon oil of known viscosity.<br />

During the so-called material preparation (see also Section 6.1.1), the semi-<strong>solid</strong><br />

material in the rheometer was generated by first completely liquefying <strong>solid</strong> material<br />

followed by cooling to the desired temperature in the mushy state at a fixed cooling<br />

rate and a shear rate of 100 s 1 . After isothermal shearing for 1 h, the experiments<br />

described in Section 6.1.5.1 were carried out.<br />

6.1.5.2 Capillary Rheometer<br />

In capillary rheometry, the fluid is extruded through a slot capillary of a circular or<br />

rectangular cross-section at a constant flow rate. When the flow reaches steady-state<br />

conditions, the pressure drop Dp along the capillary length L is measured experimentally.<br />

Hence the true shear stress at the capillary wall Dw can be determined by the<br />

following equation:<br />

tw ¼ HDp<br />

ð6:11Þ<br />

2L<br />

In terms of a slit capillary of rectangular cross-section with a flow rate Q ¼ uHW,<br />

where u is the average velocity of the slurry, H is the height and W is the width of the<br />

capillary, the apparent shear rate g_ ap can be determined by<br />

g_ ap ¼ 6Q<br />

WH2 The apparent viscosity hap of the slurry is defined as<br />

h ap ¼ tw<br />

_<br />

g ap<br />

6.1 Empirical Analysis of the Flow Behaviourj177<br />

ð6:12Þ<br />

ð6:13Þ<br />

According to Equation 6.11, the viscosity is proportional to the measured pressure<br />

drop Dp and inversely proportional to the steady-state flow rate Q. Capillary rheometry<br />

is a single-point method, that is, it only provides one viscosity value and its<br />

corresponding shear rate for each experiment. The results are extracted under highly<br />

transient conditions since the measuring time for these experiments varies in the<br />

range of seconds. Hence no steady-state values can be extracted, although the<br />

information gathered from these experiments is probably close to isostructural data.<br />

Compared with rheological studies which have been carried out using concentric<br />

cylinder rheometers (see Section 6.1.4), the length of the experimental time in<br />

capillary rheometers is orders of magnitudes smaller and the applied shear rates are<br />

orders of magnitudes higher (Table 6.1). Furthermore, experiments in rotational<br />

rheometers can be conducted under steady-state conditions and time-dependent<br />

effects can be measured using discontinuous or linear variances of the shear rate [23].

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