
Exercise 3
Velocity decomposition
We infer on an expression for the flow field given by
\[ v(x) = \begin{pmatrix} 1-y \\ 1 + x \\ 0 \end{pmatrix} \tag{1}\]
Decompose the given velocity field by calculating the axial vector of spin tensor \(\mathbf{W}\) and the strain rate tensor \(\mathbf{D}\)
Superposition of which two of the following flow fields would lead to the flow field as described in Equation 1.
| \(\boxed{\phantom{X}} \text{ A}\) | \(\boxed{\phantom{X}} \text{ B}\) | \(\boxed{\phantom{X}} \text{ C}\) | \(\boxed{\phantom{X}} \text{ D}\) |
\[\begin{multline*} \shoveright{} \textbf{Points: 4} \end{multline*}\]
- Axial vector of spin tensor \(\mathbf{W}\) \[ \mathbf{w} = \dfrac{1}{2} \nabla \times \mathbf{v} = \dfrac{1}{2} \begin{pmatrix} 0 \\ 0 \\ 1 + 1 \end{pmatrix} = \begin{pmatrix} 0 \\ 0 \\ 1 \end{pmatrix} \]
\[\begin{multline*} \shoveright{} \textbf{Points: 1} \end{multline*}\]
\[ \begin{aligned} \mathbf{D} &= \dfrac{1}{2} (\nabla \mathbf{v} + \nabla \mathbf{v}^T) \\ &= \dfrac{1}{2} \left( \begin{bmatrix} 0 & -1 & 0\\ 1 & 0 & 0\\ 0 & 0 & 0 \end{bmatrix} + \begin{bmatrix} 0 & 1 & 0\\ -1 & 0 & 0\\ 0 & 0 & 0 \end{bmatrix} \right) \\ \mathbf{D} &= \mathbf{0} \end{aligned} \]
\[\begin{multline*} \shoveright{} \textbf{Points: 1} \end{multline*}\]
- Superposition of flow fields A(pure translation) and C(pure rotation)
\[\begin{multline*} \shoveright{} \textbf{Points: 2} \end{multline*}\]
Bernoulli
The figure shows a Venturi tube, which can be used to measure fluid flow. It comprises a cylindrical inlet with cross section \(A_1\) followed by a convergent entrance into a cylindrical throat with cross section \(A_2\) and a divergent outlet. The velocity of the fluid at inlet and the throat is \(\mathbf{v}_1\) and \(\mathbf{v}_2\) respectively. The flowing fluid has density \(\rho_a\) and the liquid in the U-shaped tube has a density \(\rho_f\).

Tasks
Task 1
State the Bernoulli equation and explain to what fluid flow scenarios it can be applied.
Along a stationary flow streamline
Task 2
Calculate the velocity of the flowing fluid in terms of the difference in height of the fluid \(\Delta h\) in the U-shaped tube and other given quantities given in the figure.
To solve the problem, we need to formulate Bernoulli between the different points.
- Bernoulli between points 1 and 2: These points lie at the same height

\[ p_1 + \frac{1}{2}\,\rho_a\,v_1^2 = p_2 + \frac{1}{2}\,\rho_a\,v_2^2 \]
and thus
\[ p_1 - p_2= \frac{1}{2}\,\rho_a\,\left(\,v_2^2 - v_1^2\right) \]
- The hydrostatic pressure at the bottom of the tube can be expressed in terms of two heights:
\[ p_{\text{bottom}} = p_1 + \rho_a\,g\,d_1 + \rho_f\, g\,h_1 \quad , \]
and
\[ p_{\text{bottom}} = p_2 + \rho_a\,g\,d_2 + \rho_f\, g\,h_2 \quad . \]
Setting these equations equal yields an expression in terms of \(p_1\), \(p_2\) and the height difference \(\Delta h = h_2 - h_1\)
\[ p_1 - p_2 = \left(\rho_f - \rho_a \right)\, g \,\Delta h \]
Substituting the expression for \(p_1 -p_2\) back into the first expression for \(\Delta p = p_1 - p_2\) gives
\[ \frac{1}{2}\,\rho_a\,\left(\,v_2^2 - v_1^2\right) = \left(\rho_f - \rho_a \right)\, g \,\Delta h \quad . \]
The continuity equation for the constant density fluid yields
\[ v_2\,A_2 = v_1\,A_1 \Rightarrow v_2 = \frac{A_1}{A_2} \,v_1 \quad . \]
Substituting in the above equation yields
\[ \frac{1}{2}\,\rho_a\,\left(\,\left(\frac{A_1}{A_2}\right)^2 - 1\right)\,v_1^2 = \left(\rho_f - \rho_a \right)\,g\,\Delta h \]
which can be rearranged for \(h\) or \(v_1\) as needed.
\[ v_1 = \sqrt{\frac{2\,\left(\rho_f - \rho_a \right)\,g\,\Delta h}{\rho_a\,\left(\,\left(\frac{A_1}{A_2}\right)^2 - 1\right)}} \]