Chapter 6: Problem 16
The stream function for an incompressible, two-dimensional flow field is $$\psi=a y-b y^{3}$$ where \(a\) and \(b\) are constants. Is this an irrotational flow? Explain.
Chapter 6: Problem 16
The stream function for an incompressible, two-dimensional flow field is $$\psi=a y-b y^{3}$$ where \(a\) and \(b\) are constants. Is this an irrotational flow? Explain.
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Get started for freeAir is delivered through a constant-diameter duct by a fan. The air is inviscid, so the fluid velocity profile is "flat" across each cross section. During the fan start-up, the following velocities were measured at the time \(t\) and axial positions \(x\) : $$\begin{array}{llll} & x=0 & x=10 \mathrm{m} & x=20 \mathrm{m} \\ t=0 \mathrm{s} & V=0 \mathrm{m} / \mathrm{s} & V=0 \mathrm{m} / \mathrm{s} & V=0 \mathrm{m} / \mathrm{s} \\\t=1.0 \mathrm{s} & V=1.00 \mathrm{m} / \mathrm{s} & V=1.20 \mathrm{m} / \mathrm{s} & V=1.40 \mathrm{m} / \mathrm{s} \\\t=2.0 \mathrm{s} & V=1.70 \mathrm{m} / \mathrm{s} & V=1.80 \mathrm{m} / \mathrm{s} & V=1.90 \mathrm{m} / \mathrm{s} \\\t=3.0 \mathrm{s} & V=2.10 \mathrm{m} / \mathrm{s} & V=2.15 \mathrm{m} / \mathrm{s} & V=2.20 \mathrm{m} / \mathrm{s}\end{array}$$ Estimate the local acceleration, the convective acceleration, and the total acceleration at \(t=1.0 \mathrm{s}\) and \(x=10 \mathrm{m} .\) What is the local acceleration after the fan has reached a steady air flow rate?
An infinitely long, solid, vertical cylinder of radius \(R\) is located in an infinite mass of an incompressible fluid. Start with the Navier-Stokes equation in the \(\theta\) direction and derive an expression for the velocity distribution for the steady-flow case in which the cylinder is rotating about a fixed axis with a constant angular velocity \(\omega\). You need not consider body forces. Assume that the flow is axisymmetric and the fluid is at rest at infinity.
Two horizontal, infinite, parallel plates are spaced a distance \(b\) apart. A viscous liquid is contained between the plates. The bottom plate is fixed, and the upper plate moves parallel to the bottom plate with a velocity \(U\). Because of the no-slip boundary condition (see Video \(V 6.12\) ), the liquid motion is caused by the liquid being dragged along by the moving boundary. There is no pressure gradient in the direction of flow. Note that this is a so-called simple Couette flow discussed in Section 6.9 .2 (a) Start with the Navier-Stokes equations and determine the velocity distribution between the plates. (b) Determine an expression for the flowrate passing between the plates (for a unit width). Express your answer in terms of \(b\) and \(U\).
Blood flows at volume rate \(Q\) in a circular tube of radius \(R\). The blood cells concentrate and flow near the center of the tube. while the cell-free fluid (plasma) flows in the outer region. The center core of radius \(R_{c}\) has a viscosity \(\mu_{c}\) and the plasma has a viscosity \(\mu_{p}\). Assume laminar, fully developed flow for both the core and plasma flows and show that an "apparent" viscosity is defined by $$\mu_{\mathrm{app}}=\frac{\pi R^{4} \Delta p}{8 L Q}$$ is given by $$\mu_{\mathrm{app}}=\frac{\mu_{p}}{1-\left(R_{c} / R\right)^{4}\left(1-\mu_{p} / \mu_{c}\right)}$$
Verify that the momentum correction factor \(\beta\) for fully developed, laminar flow in a circular tube is \(4 / 3\).
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