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Computational Methods for Debonding in Composites

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300 H. Miled et al.<br />

temperature is kept constant to 130 ◦ C. The temperature balance equation is:<br />

ρCp<br />

� ∂T<br />

∂t<br />

+ v.∇T<br />

�<br />

= div(k∇T )+ ˙w (15.15)<br />

ρ is the volume density, Cp is specific heat, k is the thermal conductivity and ˙w<br />

is the viscous dissipation. These properties are considered not dependant from the<br />

<strong>in</strong>duced flow anisotropy.<br />

For short fiber re<strong>in</strong><strong>for</strong>ced materials, the flow becomes viscoelastic and the stress<br />

tensor is expressed as a function of the fourth order orientation tensor [5]:<br />

σ = 2η � ˙¯ε,T ��<br />

� ��<br />

˙ε + Np a : ˙ε − p1 (15.16)<br />

where η(˙¯ε,T ) is the temperature-dependent viscosity due to both the polymer<br />

matrix and fibers. The <strong>in</strong>duced anisotropy is represented by the parameter Np which<br />

depends on the fiber concentration and on the fiber aspect ratio, and is difficult to be<br />

predicted. Thus, its contribution to the material’s rheology is not taken <strong>in</strong>to account<br />

<strong>in</strong> this work. As a consequence, the problem is considered governed by the Navier<br />

and Stokes equations:<br />

�<br />

∂v<br />

ρ<br />

∂t +(v.∇)v<br />

�<br />

� �<br />

= −∇p + ∇. 2η ˙ε + f<br />

(15.17)<br />

∇.v = 0<br />

p is the polymer’s pressure and f are the body <strong>for</strong>ces (such as gravity). We<br />

suppose that the viscosity is given by the Carreau-Yasuda law [9, 43]:<br />

� �<br />

η(˙¯ε,T )=η0(T ) 1 + η0(T ) ˙¯ε<br />

τs<br />

�α<br />

� m−1<br />

α<br />

(15.18)<br />

where α and m are constant parameters, and η0(T ) represents the temperature<br />

dependency, follow<strong>in</strong>g the Arrhenius law:<br />

� � ��<br />

1 1<br />

η0 (T)=η0 (Tref).exp β − (15.19)<br />

T Tref<br />

The velocity-pressure mechanical problem is solved us<strong>in</strong>g the mixed f<strong>in</strong>ite element<br />

method with the P1+/P1 element and the thermal problem us<strong>in</strong>g a classical<br />

Galerk<strong>in</strong> <strong>for</strong>mulation. Both problems are weakly coupled: at each time <strong>in</strong>crement,<br />

the temperature-dependant viscosity used is the one computed at time t − ∆t. Furthermore,<br />

the position of the flow front is advected us<strong>in</strong>g a Level set technique [4].<br />

Parameters used <strong>in</strong> Eqs. 15.15, 15.18 and 15.19 are given <strong>in</strong> Table 15.1.

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