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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$.

Short Answer

Expert verified
Question: Calculate the fully developed friction coefficient at the location where the Grashof number is given as 16,600. Answer: To calculate the fully developed friction coefficient, follow the steps below: 1. Calculate the Reynolds number and the effective viscosity ratio using the given information and provided equations. 2. Determine the Nusselt number using the Gnielinski correlation and the modified Blasius correlation for the friction factor. 3. Calculate the heat transfer coefficient using the Nusselt number and the thermal conductivity of the liquid. 4. Find the fully developed friction coefficient using the relation between the heat transfer coefficient and the friction factor.

Step by step solution

01

Calculate the Reynolds number and the effective viscosity ratio

First, we need to determine the Reynolds number (\(Re\)) and the effective viscosity ratio (\(\mu_\mathrm{eff} / \mu_\mathrm{w}\)) at the location of interest. The Reynolds number can be found using the formula: $$ Re = \frac{VD}{\nu}, $$ where \(V\) is the fluid velocity, \(D\) is the inside diameter of the tube, and \(\nu\) is the kinematic viscosity of the liquid. From the given information, we can find the flow rate (\(Q = 1.43 \times 10^{-4} \mathrm{~m}^{3} / \mathrm{s}\)) and the cross-sectional area of the tube: $$ A = \frac{\pi D^2}{4} = \frac{\pi (0.0158 \mathrm{~m})^2}{4}. $$ Now, we can calculate the fluid velocity: $$ V = \frac{Q}{A}. $$ With the velocity found, we can determine the Reynolds number. As for the effective viscosity ratio, it is given as: $$ \frac{\mu_\mathrm{eff}}{\mu_\mathrm{w}} = 1 + 0.86 Re^{-0.25} \left(\frac{\mu_\mathrm{v}}{\mu_\mathrm{s}} - 1 \right), $$ where \(\mu_\mathrm{v} / \mu_\mathrm{s}\) is provided in the problem statement.
02

Calculate the Nusselt number

Next, we have to calculate the Nusselt number (\(Nu\)) using the Gnielinski correlation: $$ Nu = \frac{(f/8)(Re - 1000) Pr}{1 + 12.7(f/8)^{0.5}(Pr^{2/3} - 1)}, $$ where \(f\) is the friction factor, which can be determined using the modified Blasius correlation: $$ f = 0.078 Re^{-0.22}, $$ and \(Pr\) is the Prandtl number given in the problem statement.
03

Calculate the heat transfer coefficient

With the Nusselt number, we can calculate the heat transfer coefficient (\(h\)) using the formula: $$ h = \frac{Nu k}{D}, $$ where \(k\) is the thermal conductivity of the liquid. The thermal conductivity of the ethylene glycol-distilled water mixture can be found in the reference tables.
04

Calculate the fully developed friction coefficient

Finally, we can calculate the fully developed friction coefficient using the relation between heat transfer coefficient and friction factor: $$ \frac{h}{k} = \frac{(f/8)(Re - 1000) Pr}{1 + 12.7(f/8)^{0.5}(Pr^{2/3} - 1)}. $$ We have all the required variables to find the fully developed friction coefficient at the location where the Grashof number is given as 16,600.

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Most popular questions from this chapter

combustion gases passing through a 5 -cm-internaldiameter circular tube are used to vaporize wastewater at atmospheric pressure. Hot gases enter the tube at \(115 \mathrm{kPa}\) and \(250^{\circ} \mathrm{C}\) at a mean velocity of $5 \mathrm{~m} / \mathrm{s}\( and leave at \)150^{\circ} \mathrm{C}$. If the average heat transfer coefficient is $120 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\( and the inner surface temperature of the tube is \)110^{\circ} \mathrm{C}\(, determine \)(a)\( the tube length and \)(b)$ the rate of evaporation of water. Use air properties for the combustion gases.

Consider a fluid with a Prandtl number of 7 flowing through a smooth circular tube. Using the Colburn, Petukhov, and Gnielinski equations, determine the Nusselt numbers for Reynolds numbers at \(3500,10^{4}\), and \(5 \times 10^{5}\). Compare and discuss the results.

An ethylene glycol-distilled water mixture with a mass fraction of \(0.72\) and a flow rate of \(2.05 \times 10^{-4} \mathrm{~m}^{3} / \mathrm{s}\) flows inside a tube with an inside diameter of \(0.0158 \mathrm{~m}\) and a uniform wall heat flux boundary condition. For this flow, determine the Nusselt number at the location \(x / D=10\) for the inlet tube configuration of \((a)\) bell-mouth and \((b)\) re-entrant. Compare the results for parts \((a)\) and \((b)\). Assume the Grashof number is \(\mathrm{Gr}=60,000\). The physical properties of an ethylene glycoldistilled water mixture are $\operatorname{Pr}=33.46, \nu=3.45 \times 10^{-6} \mathrm{~m}^{2} / \mathrm{s}\(, and \)\mu_{b} / \mu_{s}=2.0$.

A 12 -m-long and 12-mm-inner-diameter pipe made of commercial steel is used to heat a liquid in an industrial process. The liquid enters the pipe with \(T_{i}=25^{\circ} \mathrm{C}, V=0.8 \mathrm{~m} / \mathrm{s}\). A uniform heat flux is maintained by an electric resistance heater wrapped around the outer surface of the pipe so that the fluid exits at \(75^{\circ} \mathrm{C}\). Assuming fully developed flow and taking the average fluid properties to be $\rho=1000 \mathrm{~kg} / \mathrm{m}^{3}, c_{p}=4000 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\(, \)\mu=2 \times 10^{-3} \mathrm{~kg} / \mathrm{m} \cdot \mathrm{s}, k=0.48 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$, and \(\mathrm{Pr}=10\), determine: (a) The required surface heat flux \(\dot{q}_{s}\), produced by the heater (b) The surface temperature at the exit, \(T_{s}\) (c) The pressure loss through the pipe and the minimum power required to overcome the resistance to flow.

Water is to be heated from \(10^{\circ} \mathrm{C}\) to \(80^{\circ} \mathrm{C}\) as it flows through a \(2-\mathrm{cm}\)-internal-diameter, \(13-\mathrm{m}\)-long tube. The tube is equipped with an electric resistance heater, which provides uniform heating throughout the surface of the tube. The outer surface of the heater is well insulated, so in steady operation all the heat generated in the heater is transferred to the water in the tube. If the system is to provide hot water at a rate of \(5 \mathrm{~L} / \mathrm{min}\), determine the power rating of the resistance heater. Also, estimate the inner surface temperature of the pipe at the exit.

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