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Thixoforming : Semi-solid Metal Processing

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<strong>Semi</strong>-<strong>solid</strong> viscosity (Pa s)<br />

into clusters able to form a stiff network. Mechanical loading is transmitted through<br />

interglobular bonds and the system behaves like a <strong>solid</strong>, leading to a high viscosity.<br />

In the calculations, the <strong>solid</strong> fraction in the active zone f s<br />

A is found to be higher than<br />

0.4. As the shear rate increases, more and more bonds between <strong>solid</strong> particles are<br />

broken, leading to a progressive decrease in f s<br />

A down to 0.4. A more dispersed<br />

suspension having a fluid-like behaviour is thus obtained and, in the calculation, a<br />

strong decrease in the active zone viscosity is observed. These results prove that the<br />

shear-thinning behaviour of semi-<strong>solid</strong> alloys is due to an evolution of the liquid–<br />

<strong>solid</strong> spatial distribution within the material. This evolution is attributed to local<br />

deformation mechanisms, namely the fact that deformation is mainly carried by the<br />

<strong>solid</strong> bonds and the non-entrapped liquid.<br />

The prediction capability of the model is tested by calculating the semi-<strong>solid</strong> steadystate<br />

viscosity for a <strong>solid</strong> fraction of 0.45, keeping all the parameters constant. Very<br />

good agreement between the calculated and experimental results (Figures 7.5 and 7.6)<br />

Table 7.1 Set of identified parameters for the Sn–15wt%Pb semi<strong>solid</strong><br />

alloy simulations of steady-state viscosities for f s ¼ 0.5.<br />

K s<br />

70<br />

60<br />

50<br />

40<br />

30<br />

20<br />

10<br />

0<br />

0<br />

50<br />

100<br />

m K dg/K ag n f A<br />

1 MPa 0.43 0.8 0.2 0.007<br />

150<br />

Shear rate (s -1 )<br />

Figure 7.6 Evolution of the semi-<strong>solid</strong> viscosity as a function of the<br />

shear rate at high shear rates for the Sn–15wt%Pb alloy.<br />

Experimental data were obtained using concentric cylinder<br />

viscometer tests.<br />

200<br />

7.4 Results and Discussionj231<br />

Joly & Mehrabian (1976) ; f s = 0.5<br />

Micro-macro modelling ; f s = 0.5<br />

Joly & Mehrabian (1976) ; f s = 0.45<br />

Mictro-macro modelling : f s = 0.45<br />

250<br />

300

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