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Thixoforming : Semi-solid Metal Processing

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Based on the <strong>solid</strong> fraction of the metallic suspension, one can distinguish between<br />

the two groups of slurries and of corresponding models. When the <strong>solid</strong> fraction in<br />

the semi-<strong>solid</strong> slurry ranges from 20 to 90%, suspensions above 60% behave as nonlinear<br />

viscoplastic <strong>solid</strong>s and are used in forging processes, and metal slurries below a<br />

<strong>solid</strong> fraction of 60% are used in casting processes and exhibit a non-Newtonian,<br />

history-dependent flow behaviour that is referred to as pseudoplasticity and thixotropy.<br />

Consequently, there are basically two groups of models to describe semi-<strong>solid</strong><br />

slurries: for highly concentrated suspensions behaving as <strong>solid</strong> bodies, models based<br />

on <strong>solid</strong> body mechanics are used; and for slurries with <strong>solid</strong> content less than 60%<br />

that behave like non-Newtonian suspensions, models based on computational fluid<br />

dynamics (CFD) are use. The models based on <strong>solid</strong> body mechanics are explained in<br />

Section 6.1.2.<br />

Models based on CFD can be classified according to whether the modelling is onephase,<br />

where the material is assumed to be continuum, or two-phase, where both<br />

liquid phase and globular particles are taken into account. Furthermore, classification<br />

can also be made based on discretization methods, that is, methods of approximating<br />

the differential equations by a system of algebraic equations such as finite element<br />

(FE), finite difference (FD) and finite volume (FV) models.<br />

Another important issue when dealing with such flows is the proper determination<br />

of the interface position in time. There are basically two methods for dealing with this<br />

issue: moving mesh strategies and fixed mesh approaches. The first group uses some<br />

form of the mesh moving strategy, such as Lagrangian or arbitrary Lagrangian–<br />

Eulerian (ALE) techniques. Due to the possibility of mesh distortion, such strategies<br />

often need to be complemented by a remeshing strategy. The second approach uses a<br />

fixed fluid mesh, supplemented by an appropriate strategy for tracking the fluid–<strong>solid</strong><br />

(fluid–air) interfaces.<br />

The main difficulty when modelling thixoforming processes is to take into account<br />

all the complex phenomena occurring within the flow. Some of the models refer to<br />

the thixotropic behaviour only, where metals are treated as homogeneous materials<br />

[32]. The others take into account the two-phase flow, but neglect the thixotropy.<br />

Other authors, while considering thixotropy, neglect the heat transfer during the<br />

process. Alexandrou et al. [33] implemented the heat transfer and the phase change<br />

together with thixotropy in a commercial simulation package, but did not take the<br />

phase segregation into account.<br />

The literature on numerical models of thixoforming was recently reviewed by<br />

Atkinson [2].<br />

6.2.2<br />

Numerical Models Used<br />

6.2 Numerical Modelling of Flow Behaviourj197<br />

6.2.2.1 Material Models<br />

The basic point of any numerical method is the mathematical model, that is, the set of<br />

partial differential or integro-differential equations and boundary conditions (an<br />

appropriate model for the target application, incompressible, inviscid, turbulent; two-

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