Warning: foreach() argument must be of type array|object, bool given in /var/www/html/web/app/themes/studypress-core-theme/template-parts/header/mobile-offcanvas.php on line 20

Consider laminar flow in a circular tube. Will the friction factor be higher near the inlet of the tube or near the exit? Why? What would your response be if the flow were turbulent?

Short Answer

Expert verified
Answer: In laminar flow, the friction factor is higher near the inlet and lower near the exit due to the developing velocity profile. In turbulent flow, there is no significant difference in the friction factor near the inlet and exit of the tube.

Step by step solution

01

Understand laminar flow and friction factor

Laminar flow is a type of flow in which fluid particles move in smooth, parallel layers without much mixing between layers. In laminar flow, the friction factor depends on the Reynolds number (Re), which is the ratio of inertial forces to viscous forces within the fluid. The friction factor (f) for a circular tube can be calculated using the Hagen-Poiseuille equation: f = \frac{16}{Re} where Re = \frac{ρuD}{μ}, with ρ being the fluid density, u the fluid velocity, D the diameter of the tube, and μ the dynamic viscosity of the fluid.
02

Discuss friction factor in laminar flow near the inlet and exit

As fluid enters the tube, the velocity profile is not fully developed, which means that the velocity near the wall is higher compared to a fully developed flow. Since the friction factor depends on the Reynolds number (which involves fluid velocity), it might vary near the inlet of the tube. As the flow becomes fully developed further downstream, the velocity profile becomes parabolic, and the friction force between the layers becomes more constant and uniform. Based on this, we expect the friction factor to be higher near the inlet of the tube and lower near the exit in laminar flow.
03

Understand turbulent flow and its effect on the friction factor

Turbulent flow is characterized by the random and chaotic motion of fluid particles, leading to significant mixing between layers. The friction factor in turbulent flow also depends on the Reynolds number, but the relationship is more complex and can be approximated by empirical formulas such as the Colebrook equation: \frac{1}{\sqrt{f}} = -2\log_{10}\left(\frac{\varepsilon}{3.7D} + \frac{2.51}{Re\sqrt{f}}\right) where ε is the roughness of the tube.
04

Discuss friction factor in turbulent flow near the inlet and exit

In turbulent flow, the velocity profile is more uniform throughout the tube, and the flow is dominated by random fluctuations. The friction factor depends on both the Reynolds number and the roughness of the tube walls. Therefore, the friction factor would not show significant variation near the inlet and exit of the tube for turbulent flow, but the overall friction factor would be higher in turbulent flow compared to laminar flow due to increased mixing and energy dissipation. In conclusion, for laminar flow, the friction factor is higher near the inlet and lower near the exit, whereas for turbulent flow, there is no significant difference in the friction factor near the inlet and exit.

Unlock Step-by-Step Solutions & Ace Your Exams!

  • Full Textbook Solutions

    Get detailed explanations and key concepts

  • Unlimited Al creation

    Al flashcards, explanations, exams and more...

  • Ads-free access

    To over 500 millions flashcards

  • Money-back guarantee

    We refund you if you fail your exam.

Over 30 million students worldwide already upgrade their learning with Vaia!

One App. One Place for Learning.

All the tools & learning materials you need for study success - in one app.

Get started for free

Most popular questions from this chapter

Water at $10^{\circ} \mathrm{C}\left(\rho=999.7 \mathrm{~kg} / \mathrm{m}^{3}\right.\( and \)\mu=1.307 \times\( \)10^{-3} \mathrm{~kg} / \mathrm{m} \cdot \mathrm{s}\( ) is flowing in a \)0.20-\mathrm{cm}$-diameter, 15 -m-long pipe steadily at an average velocity of $1.2 \mathrm{~m} / \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? Answers: (a) \(188 \mathrm{kPa}\), (b) $0.71 \mathrm{~W}$

Hot water at \(90^{\circ} \mathrm{C}\) enters a \(15-\mathrm{m}\) section of a cast iron pipe \((k=52 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) whose inner and outer diameters are 4 and \(4.6 \mathrm{~cm}\), respectively, at an average velocity of \(1.2 \mathrm{~m} / \mathrm{s}\). The outer surface of the pipe, whose emissivity is \(0.7\), is exposed to the cold air at $10^{\circ} \mathrm{C}\( in a basement, with a convection heat transfer coefficient of \)12 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. Taking the walls of the basement to be at \(10^{\circ} \mathrm{C}\) also, determine \((a)\) the rate of heat loss from the water and (b) the temperature at which the water leaves the basement.

In a food processing plant, hot liquid water is being transported in a pipe \((k=15 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), $D_{i}=2.5 \mathrm{~cm}, D_{o}=3 \mathrm{~cm}\(, and \)L=10 \mathrm{~m}$.) The hot water flowing with a mass flow rate of \(0.15 \mathrm{~kg} / \mathrm{s}\) enters the pipe at \(100^{\circ} \mathrm{C}\) and exits at \(60^{\circ} \mathrm{C}\). The plant supervisor thinks that since the hot water exits the pipe at $60^{\circ} \mathrm{C}$, the pipe's outer surface temperature should be safe from thermal burn hazards. In order to prevent thermal burn upon accidental contact with skin tissue for individuals working in the vicinity of the pipe, the pipe's outer surface temperature should be kept below \(45^{\circ} \mathrm{C}\). Determine whether or not there is a risk of thermal burn on the pipe's outer surface. Assume the pipe outer surface temperature remains constant.

In a thermal system, water enters a \(25-\mathrm{mm}\)-diameter and \(23-\mathrm{m}\)-long circular tube with a mass flow rate of $0.1 \mathrm{~kg} / \mathrm{s}\( at \)25^{\circ} \mathrm{C}$. The heat transfer from the tube surface to the water can be expressed in terms of heat flux as \(\dot{q}_{s}(x)=a x\). The coefficient \(a\) is $400 \mathrm{~W} / \mathrm{m}^{3}\(, and the axial distance from the tube inlet is \)x$ measured in meters. Determine \((a)\) an expression for the mean temperature \(T_{m}(x)\) of the water, \((b)\) the outlet mean temperature of the water, and (c) the value of a uniform heat flux \(\dot{q}_{s}\) on the tube surface that would result in the same outlet mean temperature calculated in part (b). Evaluate water properties at \(35^{\circ} \mathrm{C}\).

The exhaust gases of an automotive engine leave the combustion chamber and enter an 8 -ft-long and 3.5-in-diameter thin-walled steel exhaust pipe at \(800^{\circ} \mathrm{F}\) and \(15.5 \mathrm{psia}\) at a rate of $0.05 \mathrm{lbm} / \mathrm{s}$. The surrounding ambient air is at a temperature of \(80^{\circ} \mathrm{F}\), and the heat transfer coefficient on the outer surface of the exhaust pipe is $3 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2},{ }^{\circ} \mathrm{F}$. Assuming the exhaust gases to have the properties of air, determine \((a)\) the velocity of the exhaust gases at the inlet of the exhaust pipe and \((b)\) the temperature at which the exhaust gases will leave the pipe and enter the air.

See all solutions

Recommended explanations on Physics Textbooks

View all explanations

What do you think about this solution?

We value your feedback to improve our textbook solutions.

Study anywhere. Anytime. Across all devices.

Sign-up for free