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The velocity profile in fully developed laminar flow in a circular pipe of inner radius \(R=10 \mathrm{~cm}\), in \(\mathrm{m} / \mathrm{s}\), is given by \(u(r)=4\left(1-r^{2} / R^{2}\right)\). Determine the mean and maximum velocities in the pipe, and determine the volume flow rate.

Short Answer

Expert verified
Answer: The maximum velocity is 4 m/s, the mean velocity is 2/30 m/s, and the volume flow rate is π/300 m³/s.

Step by step solution

01

Identifying given values

We are given the following information and formulas: - The inner radius of the pipe, \(R = 10 \mathrm{~cm} = 0.1 \mathrm{~m}\) - The velocity profile, \(u(r)=4\left(1-\frac{r^2}{R^2}\right)\)
02

Find the maximum velocity

To find the max velocity, we need to find the point where the derivative of the velocity profile with respect to the radius, \(r\), is zero. So, $$ \frac{du(r)}{dr} = \frac{d}{dr}\left[4\left(1-\frac{r^2}{R^2}\right)\right] $$ Now let's find the derivative: $$ \frac{du(r)}{dr} = -\frac{8r}{R^2} $$ We can see that the derivative will be zero when \(r = 0\). So, the maximum velocity occurs at the center of the pipe (i.e., \(r = 0\)). Now let's find the maximum velocity \(u_{max}\) by inserting \(r = 0\) in the velocity profile equation: $$ u_{max} = u(0) = 4\left(1-\frac{0^2}{R^2}\right) = 4 \mathrm{~m/s} $$
03

Find the mean velocity

To find the mean velocity, we need to first calculate the integral of the velocity profile over the entire cross-sectional area of the pipe, and then divide by the total area. The cross-sectional area of the pipe is given by \(A = \pi R^2\). So, the mean velocity \(u_{mean}\) can be calculated as follows: $$ u_{mean} = \frac{1}{A}\int_{0}^{R} u(r) 2\pi r dr $$ Now let's insert the given velocity profile and solve the integral: $$ u_{mean} = \frac{1}{\pi R^2}\int_{0}^{R} 4\left(1-\frac{r^2}{R^2}\right) 2\pi r dr $$ $$ u_{mean} = \frac{8}{R^2}\int_{0}^{R} (R^2 - r^2) r dr $$ Now calculate the integral: $$ u_{mean} = \frac{8}{R^2}\left[\frac{1}{4}R^4 - \frac{1}{12}R^4\right] = \frac{8}{R^2}\left[\frac{1}{12}R^4\right] = \frac{2}{3}R^2 $$ Now substitute the radius \(R=0.1\,\mathrm{m}\) and find the mean velocity: $$ u_{mean} = \frac{2}{3}(0.1^2) = \frac{2}{30} \mathrm{~m/s} $$
04

Find the volume flow rate

The volume flow rate, \(Q\), can be calculated as the product of the mean velocity and the pipe's cross-sectional area: $$ Q = u_{mean} A $$ Now substitute the mean velocity and the area, and calculate \(Q\): $$ Q = \left(\frac{2}{30} \mathrm{~m/s}\right)\left( \pi(0.1^2)\right) = \frac{\pi}{300} \mathrm{~m^3/s} $$ In conclusion, the maximum velocity in the pipe is \(4 \mathrm{~m/s}\), the mean velocity is \(\frac{2}{30} \mathrm{~m/s}\), and the volume flow rate is \(\frac{\pi}{300} \mathrm{~m^3/s}\).

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Most popular questions from this chapter

A liquid hydrocarbon enters a \(2.5\)-cm-diameter tube that is \(5.0 \mathrm{~m}\) long. The liquid inlet temperature is \(20^{\circ} \mathrm{C}\) and the tube wall temperature is \(60^{\circ} \mathrm{C}\). Average liquid properties are $c_{p}=2.0 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}, \mu=10 \mathrm{mPa} \cdot \mathrm{s}\(, and \)\rho=900 \mathrm{~kg} / \mathrm{m}^{3}$. At a flow rate of \(1200 \mathrm{~kg} / \mathrm{h}\), the liquid outlet temperature is measured to be \(30^{\circ} \mathrm{C}\). Estimate the liquid outlet temperature when the flow rate is reduced to \(400 \mathrm{~kg} / \mathrm{h}\). Hint: For heat transfer in tubes, \(\mathrm{Nu} \propto \mathrm{Re}^{1 / 3}\) in laminar flow and \(\mathrm{Nu} \propto \mathrm{Re}^{4 / 5}\) in turbulent flow.

A tube with a square-edged inlet configuration is subjected to uniform wall heat flux of \(8 \mathrm{~kW} / \mathrm{m}^{2}\). The tube has an inside diameter of \(0.622\) in and a flow rate of \(2.16 \mathrm{gpm}\). The liquid flowing inside the tube is an ethylene glycol-distilled water mixture with a mass fraction of \(2.27\). Determine the friction coefficient at a location along the tube where the Grashof number is Gr \(=35,450\). The physical properties of the ethylene glycol-distilled water mixture at the location of interest are $\operatorname{Pr}=13.8, \nu=18.4 \times 10^{-6} \mathrm{ft}^{2} / \mathrm{s}\(, and \)\mu_{b} / \mu_{s}=1.12$. Then recalculate the fully developed friction coefficient if the volume flow rate is increased by 50 percent while the rest of the parameters remain unchanged.

Liquid water flows in a circular tube at a mass flow rate of $0.12 \mathrm{~kg} / \mathrm{s}\(. The water enters the tube at \)65^{\circ} \mathrm{C}\(, where it is heated at a rate of \)5.5 \mathrm{~kW}$. The tube is circular with a length of \(3 \mathrm{~m}\) and an inner diameter of $25 \mathrm{~mm}$. The tube surface is maintained isothermal. The inner surface of the tube is lined with polyvinylidene chloride (PVDC) lining. The recommended maximum temperature for PVDC lining is \(79^{\circ} \mathrm{C}\) (ASME Code for Process Piping, ASME B31.3-2014, Table A323.4.3). Is the PVDC lining suitable for the tube under these conditions? Evaluate the fluid properties at \(70^{\circ} \mathrm{C}\). Is this an appropriate temperature at which to evaluate the fluid properties?

Consider a 25-mm-diameter and 15-m-long smooth tube that is maintained at a constant surface temperature. Fluids enter the tube at \(50^{\circ} \mathrm{C}\) with a mass flow rate of \(0.01 \mathrm{~kg} / \mathrm{s}\). Determine the tube surface temperatures necessary to heat water, engine oil, and liquid mercury to the desired outlet temperature of \(150^{\circ} \mathrm{C}\).

Water at $15^{\circ} \mathrm{C}\left(\rho=999.1 \mathrm{~kg} / \mathrm{m}^{3}\right.\( and \)\mu=1.138 \times 10^{-3}\( \)\mathrm{kg} / \mathrm{m} \cdot \mathrm{s}\( ) is flowing in a \)4-\mathrm{cm}$-diameter and \(25-\mathrm{m}\)-long horizontal pipe made of stainless steel steadily at a rate of \(7 \mathrm{~L} / \mathrm{s}\). Determine \((a)\) the pressure drop and \((b)\) the pumping power requirement to overcome this pressure drop. Assume flow is fully developed. Is this a good assumption?

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