Darcy fingering equations#
Governing equations for miscible viscous fingering in Darcy flow.
Dimensional equations#
Non-dimensionalization#
Scalings#
Quantity |
\(\vert\textbf{x}\vert\) |
\(\vert\textbf{u}\vert\) |
\(t\) |
\(c\) |
\(p\) |
\(\psi\) |
\(\mu\) |
\(\phi\) |
\(K\) |
\(\vert\mathsf{D}\vert\) |
|---|---|---|---|---|---|---|---|---|---|---|
Scaling |
\(\mathcal{L}\) |
\(\mathcal{U}\) |
\(\mathcal{T}\) |
\(\Delta c\) |
\(\mu_{\text{ref}}\,\mathcal{U}\mathcal{L}/K_{\text{ref}}\) |
\(\mathcal{U}\mathcal{L}\) |
\(\mu_{\text{ref}}\) |
\(\phi_{\text{ref}}\) |
\(K_{\text{ref}}\) |
\(D_{\text{ref}}\) |
Generic dimensionless numbers#
Physical dimensionless numbers#
Definition |
Name |
Physical interpretation |
|---|---|---|
\(Pe=\frac{\vert\textbf{u}_{\text{in}}\vert\mathcal{L}_\Omega}{D_{\text{ref}}}\) |
Peclet number |
Ratio of injection to diffusive speeds. |
\(P_\Delta=\frac{K_{\text{ref}}\Delta p}{D_{\text{ref}}\mu_{\text{ref}}}\) |
pressure Peclet number |
Peclet number for pressure-driven flow. |
Scaling choice#
Name |
\(\mathcal{L}\) |
\(\mathcal{U}\) |
\(\mathcal{T}\) |
\(Ad\) |
\(Di\) |
\(In\) |
\(X\) |
|---|---|---|---|---|---|---|---|
advective |
\(\mathcal{L}_\Omega\) |
\(\lvert\mathbf{u}_{\text{in}}\rvert\) |
\(\phi_{\text{ref}}\mathcal{L}/\mathcal{U}\) |
\(1\) |
\(1/Pe\) |
\(1\) |
\(1\) |
diffusive |
\(\mathcal{L}_\Omega\) |
\(D_{\text{ref}}/\mathcal{L}\) |
\(\phi_{\text{ref}}\mathcal{L}/\mathcal{U}\) |
\(1\) |
\(1\) |
\(Pe\) |
\(1\) |
pressure-driven |
\(\mathcal{L}_\Omega\) |
\(K_{\text{ref}}\Delta p/\mathcal{L}\mu_{\text{ref}}\) |
\(\phi_{\text{ref}}\mathcal{L}/\mathcal{U}\) |
\(1\) |
\(1/P_\Delta\) |
\(0\) |
\(1\) |