30.01.2013 Views

Thixoforming : Semi-solid Metal Processing

Thixoforming : Semi-solid Metal Processing

Thixoforming : Semi-solid Metal Processing

SHOW MORE
SHOW LESS

You also want an ePaper? Increase the reach of your titles

YUMPU automatically turns print PDFs into web optimized ePapers that Google loves.

198j 6 Modelling the Flow Behaviour of <strong>Semi</strong>-<strong>solid</strong> <strong>Metal</strong> Alloys<br />

or three-dimensional, etc.) [34]. Here, the one- and two-phase models based on the<br />

Herschel–Bulkley approach will be presented.<br />

One-phase Model The thixotropic model applied is based on an approach initially<br />

suggested by Moore [19] and described in Section 6.1.2.1. The model, which includes<br />

a finite yield stress, is composed of semi-<strong>solid</strong> alloys at different <strong>solid</strong> fractions and is<br />

fitted to experimental data [35]. The shear stress is defined as a function of shear rate<br />

and a time-dependent structural parameter, describing the structural influence on<br />

the flow behaviour, such as the current state of agglomeration. Furthermore, the<br />

shear stress is assumed to grow exponentially with increasing <strong>solid</strong> fraction.<br />

Two-phase Model This numerical approach is based on a two-phase modified<br />

Herschel–Bulkley model, considering the yield stress, shear thinning and thixotropic<br />

behaviour (see Section 6.1.2.1). It describes the metal alloy as a mixture of a<br />

continuous matrix liquid phase and dispersed <strong>solid</strong> particles regarded as a pseudo-continuum.<br />

The mathematical model uses the two-phase approach, with two sets<br />

of conservation equations for the bulk and liquid phases, where the relation between<br />

<strong>solid</strong> and liquid phase is modelled by Darcy s law [9]. The mass and momentum<br />

conservation equations are solved for the bulk and liquid phases. The mass<br />

conservation equation of the bulk phase is<br />

r _ u _ ¼ 0 ð6:16Þ<br />

The velocity u is defined as the sum of the velocities of individual phases (uS, <strong>solid</strong><br />

phase velocity; uL, liquid phase velocity) weighted by the corresponding fractions of<br />

<strong>solid</strong>, fS, and liquid, fL:<br />

u_ ¼ f u S _ S þ f Lu_ L ð6:17Þ<br />

The bulk flow is governed by the general momentum conservation equation in the<br />

classical form:<br />

Du_ r<br />

Dt ¼ r_ p þ r S<br />

_ _ þ rg<br />

_ ð6:18Þ<br />

with the <strong>solid</strong>-phase density rS, the liquid phase density rL and the isotropic pressure<br />

p; g is the acceleration due to gravity. The non-Newtonian flow behaviour is expressed<br />

by the extra stress tensor S:<br />

S _ ¼ 2h B D _ ð6:19Þ<br />

where D is the deformation rate tensor and hB describes the viscosity of the bulk<br />

phase (Equation 6.1). For the liquid phase, the momentum conservation equation has<br />

the following form:<br />

r L<br />

D f u L _ L<br />

Dt<br />

¼ f L r _ p þ r _ f L S _ L þ r L f L g _ þ q _<br />

ð6:20Þ

Hooray! Your file is uploaded and ready to be published.

Saved successfully!

Ooh no, something went wrong!