Viscous flow down an incline ============================ Goals ----- - Present the equations of linear viscous flow down an inclined plane Linear viscous flow ------------------- .. figure:: img/Allen_fig_4-12a.png :width: 600px :align: center :alt: Viscous flow down an incline Figure 1. Viscous flow down an incline Shear stress in the fluid ~~~~~~~~~~~~~~~~~~~~~~~~~ For a fluid flowing down an inclined slope, the change in potential energy per unit area of the contact surface along some length of the slope :math:`\delta x` is .. math:: \begin{align} \Delta E_{\mathrm{P}} &= \rho g h \delta z\\ &= \rho g h (\bar{u} S) \end{align} where :math:`\Delta E_{\mathrm{P}}` is the change in potential energy, :math:`\rho` is the fluid density, :math:`g` is the acceleration due to gravity, :math:`h` is the thickness of the flow, :math:`\delta z` is the elevation change over the distance :math:`x`\ , :math:`\bar{u}` is the average flow velocity, and :math:`S` is the slope of the incline. .. figure:: img/Allen_fig_4-12b.png :width: 600px :align: center :alt: Viscous flow down an incline Figure 2. Viscous flow down an incline The downslope component of the gravity force on the flow is thus :math:`\rho g h S`\ , which must be opposed by the drag force at the base of the flow :math:`\tau_{0}`\ . Thus, we can say .. math:: \tau_{0} = \rho g h S We can also calculate the shear stress for any position :math:`z` above the base of the flow, which is a function of the thickness of the overlying fluid :math:`(h - z)` .. math:: \begin{align} \tau_{z} &= \rho g S (h - z) && \text{Since we know that }\tau_{0} = \rho g h S\\ \tau_{z} &= \tau_{0} \left( 1 - \frac{z}{h} \right) \end{align} .. attention:: What does this suggest about the shear strength as a function of depth in the fluid? Linking to viscous flow ~~~~~~~~~~~~~~~~~~~~~~~ For a laminar flow, we know :math:`\tau = \eta du/dz`\ , so we can rewrite the resistance equation as .. math:: \begin{align} \tau_{z} &= \eta \frac{du}{dz}\\ \tau_{z} &= \rho g S (h - z)\\ \eta \frac{du}{dz} &= \rho g S (h - z)\\ \frac{du}{dz} &= \frac{\rho g S (h - z)}{\eta}\\ \frac{du}{dz} &= \frac{\rho g S}{\eta} (h - z) \end{align} If we integrate this equation with respect to :math:`z`\ , we find .. math:: \begin{align} \int \frac{du}{dz} &= \frac{\rho g S}{\eta} \int (h - z)\\ u &= \frac{\rho g S}{\eta} \left(zh - \frac{z^{2}}{2} \right) + c_{1} \end{align} If we assume the flow velocity :math:`u = 0` at :math:`z = 0` (the base of the flow), the constant :math:`c_{1} = 0`\ , so we are left with .. math:: u = \frac{\rho g S}{\eta} \left(zh - \frac{z^{2}}{2} \right) .. attention:: - What would the velocity profile look like in this flow? - Where is the maximum velocity? - What happens if the viscosity decreases? Slope increases? Thickness increases? Viscous flow take-home messages ------------------------------- - The flow is a balance between the gravitational force on the fluid and resistance (drag) at the base - The flow velocity increases following a parabolic geometry from :math:`u = 0` at the base to :math:`\frac{\rho g S}{\eta} \frac{z^{2}}{2}` Caveats ------- - Steady-state - 1-D - Laminar flow! - Constants are constant - No temperature dependence