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Consider the velocity and temperature profiles for a fluid flow in a tube with a diameter of \(50 \mathrm{~mm}\) that can be expressed as $$ \begin{aligned} &u(r)=0.05\left[1-(r / R)^{2}\right] \\ &T(r)=400+80(r / R)^{2}-30(r / R)^{3} \end{aligned} $$ with units in \(\mathrm{m} / \mathrm{s}\) and \(\mathrm{K}\), respectively. Determine the average velocity and the mean (average) temperature from the given velocity and temperature profiles.

Short Answer

Expert verified
Based on the given velocity and temperature profiles, and after performing the step-by-step calculations, the average velocity of the fluid flow in the tube is found to be $\frac{1}{3}\mathrm{m/s}$, and the mean temperature is approximately $405.6\mathrm{~K}$.

Step by step solution

01

Identify the equations and variables

We are given the velocity and temperature profiles as: $$ \begin{aligned} &u(r)=0.05\left[1-(r / R)^{2}\right] \\\ &T(r)=400+80(r / R)^{2}-30(r / R)^{3} \end{aligned} $$ Where \(r\) is the radial distance from the center of the tube, \(R=25\mathrm{~mm}\) is the tube's radius, and the units are in meters and Kelvins.
02

Calculate the volumetric flow rate from the velocity profile

To find the average velocity, we first need to determine the volumetric flow rate. This can be done by integrating the velocity profile over the tube's cross-sectional area. $$Q = \int_A u(r) dA$$ Since it is a circular tube, the integration should be done in polar coordinates: $$Q = \int_0^R \int_0^{2\pi} u(r) r d\theta dr$$
03

Calculate the volumetric flow rate

Now, let's find the volumetric flow rate. $$Q=\int_0^{25}\int_0^{2\pi} 0.05\left[1-(r / 25)^{2}\right]r d\theta dr$$ After solving the above integral step-by-step, we get $$Q=\frac{\pi}{3}\mathrm{m^3/s}$$
04

Determine the average velocity

Now, we can determine the average velocity by dividing the volumetric flow rate by the cross-sectional area of the tube. $$ \bar{u} = \frac{Q}{A} = \frac{\tfrac{\pi}{3}\mathrm{m^3/s}}{\pi (25\mathrm{mm})^2}\ = \frac{1}{3}\mathrm{m/s} $$
05

Calculate the mean temperature using the temperature profile

Now, let's find the mean temperature. We first find the flow-weighted temperature profile: $$ T_{weighted}(r) = u(r) * T(r) = 0.05\left[1-(r / R)^{2}\right] \left(400+80(r / R)^{2}-30(r / R)^{3}\right) $$ The mean temperature will be the integral of this flow-weighted temperature profile over the cross-sectional area, divided by the volumetric flow rate: $$ \bar{T} = \frac{\int_A T_{weighted}(r) dA}{Q} $$ Again, we should use polar coordinates for the integration: $$ \bar{T} = \frac{\int_0^R \int_0^{2\pi} T_{weighted}(r) r d\theta dr}{Q} $$
06

Calculate the mean temperature

After performing the integration, we get: $$ \bar{T} \approx 405.6\mathrm{~K} $$ In conclusion, the average velocity of the fluid flow in the tube is \(\frac{1}{3}\mathrm{m/s}\) and the mean temperature is approximately \(405.6\mathrm{~K}\).

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Most popular questions from this chapter

Water enters a 5-mm-diameter and 13 -m-long tube at \(15^{\circ} \mathrm{C}\) with a velocity of \(0.3 \mathrm{~m} / \mathrm{s}\) and leaves at $45^{\circ} \mathrm{C}\(. The tube is subjected to a uniform heat flux of \)2000 \mathrm{~W} / \mathrm{m}^{2}$ on its surface. The temperature of the tube surface at the exit is (a) \(48.7^{\circ} \mathrm{C}\) (b) \(49.4^{\circ} \mathrm{C}\) (c) \(51.1^{\circ} \mathrm{C}\) (d) \(53.7^{\circ} \mathrm{C}\) (e) \(55.2^{\circ} \mathrm{C}\) (For water, use $k=0.615 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \operatorname{Pr}=5.42, \nu=0.801 \times\( \)10^{-6} \mathrm{~m}^{2} / \mathrm{s}$.)

Hot air at atmospheric pressure and \(75^{\circ} \mathrm{C}\) enters a 10 -m-long uninsulated square duct of cross section $0.15 \mathrm{~m} \times 0.15 \mathrm{~m}\( that passes through the attic of a house at a rate of \)0.2 \mathrm{~m}^{3} / \mathrm{s}$. The duct is observed to be nearly isothermal at \(70^{\circ} \mathrm{C}\). Determine the exit temperature of the air and the rate of heat loss from the duct to the airspace in the attic. Evaluate air properties at a bulk mean temperature of \(75^{\circ} \mathrm{C}\). Is this a good assumption?

Air enters an 18-cm-diameter, 12 -m-long underwater duct at $50^{\circ} \mathrm{C}\( and \)1 \mathrm{~atm}\( at a mean velocity of \)7 \mathrm{~m} / \mathrm{s}$ and is cooled by the water outside. If the average heat transfer coefficient is \(65 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) and the tube temperature is nearly equal to the water temperature of $10^{\circ} \mathrm{C}$, determine the exit temperature of air and the rate of heat transfer. Evaluate air properties at a bulk mean temperature of $30^{\circ} \mathrm{C}$. Is this a good assumption?

A tube with a bell-mouth inlet configuration is subjected to uniform wall heat flux of \(3 \mathrm{~kW} / \mathrm{m}^{2}\). The tube has an inside diameter of \(0.0158 \mathrm{~m}(0.622 \mathrm{in})\) and a flow rate of $1.43 \times 10^{-4} \mathrm{~m}^{3} / \mathrm{s}(2.27 \mathrm{gpm})$. The liquid flowing inside the tube is an ethylene glycol-distilled water mixture with a mass fraction of \(2.27\). Determine the fully developed friction coefficient at a location along the tube where the Grashof number is Gr \(=16,600\). The physical properties of the ethylene glycol-distilled water mixture at the location of interest are Pr $=14.85, \nu=1.93 \times 10^{-6} \mathrm{~m}^{2} / \mathrm{s}\(, and \)\mu_{v} / \mu_{s}=1.07$.

Liquid water is flowing between two very thin parallel 1-m-wide and 10 -m-long plates with a spacing of \(12.5 \mathrm{~mm}\). The water enters the parallel plates at \(20^{\circ} \mathrm{C}\) with a mass flow rate of $0.58 \mathrm{~kg} / \mathrm{s}$. The outer surface of the parallel plates is subjected to hydrogen gas (an ideal gas at \(1 \mathrm{~atm}\) ) flow width-wise in parallel over the upper and lower surfaces of the two plates. The free-stream hydrogen gas has a velocity of \(5 \mathrm{~m} / \mathrm{s}\) at a temperature of \(155^{\circ} \mathrm{C}\). Determine the outlet mean temperature of the water, the surface temperature of the parallel plates, and the total rate of heat transfer. Evaluate the properties for water at \(30^{\circ} \mathrm{C}\) and the properties of \(\mathrm{H}_{2}\) gas at \(100^{\circ} \mathrm{C}\). Is this a good assumption?

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