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 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 \(\mathrm{Gr}=\) 16,600 . The physical properties of the ethylene glycol-distilled water mixture at the location of interest are \(\operatorname{Pr}=14.85, \nu=\) \(1.93 \times 10^{-6} \mathrm{~m}^{2} / \mathrm{s}\), and \(\mu_{b} / \mu_{s}=1.07\).

Short Answer

Expert verified
Answer: The fully developed friction coefficient is approximately 0.01910.

Step by step solution

01

1. Calculate the Grashof Number

Given in the exercise is the Grashof number: \(\mathrm{Gr} =\) 16,600. We will use this value later in the analysis.
02

2. Determine the Reynolds number.

We can find the Reynolds number using the flow rate \((Q)\), the kinematic viscosity \((\nu)\), and the diameter of the tube \((D)\), using the relation: $$\textit{Re} = \frac{4Q}{\pi D \nu}.$$ For our problem, we have \(Q = 1.43 \times 10^{-4} \mathrm{~m}^{3} / \mathrm{s}\), \(D = 0.0158 \mathrm{~m}\), and \(\nu = 1.93 \times 10^{-6} \mathrm{~m}^{2} / \mathrm{s}\). Plugging these values, we get: $$\textit{Re} = \frac{4(1.43 \times 10^{-4})}{\pi(0.0158)(1.93 \times 10^{-6})} \approx 1026.$$
03

3. Calculate the buoyancy adjusted Reynolds number.

Use the given ratio of \(\mu_b/\mu_s = 1.07\) (bulk viscosity to surface viscosity) to calculate the buoyancy adjusted Reynolds number by the following equation: $$\textit{Re}_b = \textit{Re}(\frac{\mu_b}{\mu_s}) = 1026(1.07) \approx 1097.81.$$
04

4. Determining the friction factor.

Now, with the given Prandtl number of the fluid, \(\operatorname{Pr} = 14.85\), we can use the Grashof number \((\mathrm{Gr})\) and the buoyancy adjusted Reynolds number \((\textit{Re}_b)\) to calculate the fully developed friction factor \((f)\), given by the Petukhov-Kirillov equation: $$f = \frac{0.79 \operatorname{ln}\left(\textit{Re}_b\right) - 1.64}{\textit{Re}_b} \left[1+\textstyle\frac{185}{\textit{Re}_b^{1.5}} \frac{\mathrm{Gr}}{\textit{Re}_b \operatorname{Pr}}\right]^{\frac{1}{0.3}}.$$ Substituting the given values and simplifying, we get: $$f = \frac{0.79 \operatorname{ln}\left(1097.81\right) - 1.64}{1097.81} \left[1+\frac{185}{1097.81^{1.5}} \frac{16600}{1097.81 \times 14.85}\right]^{\frac{1}{0.3}} \approx 0.01910.$$ The fully developed friction coefficient at the location along the tube with Grashof number 16,600 is 0.01910.

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Most popular questions from this chapter

A concentric annulus tube has inner and outer diameters of \(25 \mathrm{~mm}\) and \(100 \mathrm{~mm}\), respectively. Liquid water flows at a mass flow rate of \(0.05 \mathrm{~kg} / \mathrm{s}\) through the annulus with the inlet and outlet mean temperatures of \(20^{\circ} \mathrm{C}\) and \(80^{\circ} \mathrm{C}\), respectively. The inner tube wall is maintained with a constant surface temperature of \(120^{\circ} \mathrm{C}\), while the outer tube surface is insulated. Determine the length of the concentric annulus tube. Assume flow is fully developed.

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