
Titanium alloys: modelling of microstructure212
If the interface mobility M is very high, ∆
µ
V
can be very small and
CC
i
eq
≈
β
.
Under these circumstances, there is effectively local equilibrium at the interface.
The interface will then move as fast as diffusion allows, and growth will take
place under diffusion control. The growth rate then can be evaluated as a
function of time t by solving the diffusion equation in the area occupied by
the β phase with the boundary condition at the α/β interface given by
CC
i
eq
=
β
[8.21]
When the interface has a lower mobility, a greater chemical potential difference
∆
µ
V
is required to drive the interface reaction and there will be a departure
from the local equilibrium at the interface. The value of C
i
will be that which
satisfies the flux balance equation Eq. [8.14]. The growth rate then can be
evaluated by solving the diffusion equation in the area occupied by the β
phase with the boundary condition at the α/β interface given by Eq. [8.17].
8.4.3 Localisation of the α/β interface
The most important task in the analysis of the β to α transformation is the
determination of the location of the moving α/β interfaces for all of the
Widmanstätten α plates. Methods employed to solve such a problem can be
classified into two groups: Lagrangian and Eulerian schemes. The Lagrangian
scheme is characterised by the mesh which is moved or deformed with the
progress of the calculation. The mesh boundaries coincide with the free
surface. However, over-distorted meshes due to the growth of the great number
of Widmanstätten α plates in different directions may result in numerical
errors. In Eulerian schemes, computational meshes are generated beforehand
and fixed during the entire calculation. Therefore, they are free from the
difficulties due to the deforming of meshes. However, a special treatment is
necessary to track the moving free surface. The volume of fluid (VOF)
method, introduced by Hirt and Nichols, is popular in flow problems with
moving free surface. In this method, the entire domain is divided into cells
and the volume fraction of fluid in each cell is defined. The flow front is
advanced by solving the following transport equation:
∂
∂
∇⋅
F
t
F + ( ) = 0v
[8.22]
Here F is the volume fraction of the fluid in a cell and v is the flow velocity
vector.
A computer code based on the finite element method and the VOF method
is developed to trace the moving α/β interface. Instead of fluid, we consider
the volume fraction F of the α phase in the finite elements. Depending on the
value of the α phase volume fraction F in an element, the entire domain is
divided into three categories by the following criterion: