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

How are the average friction and heat transfer coefficients determined in flow over a flat plate?

Short Answer

Expert verified
Question: Explain the process of determining the average friction and heat transfer coefficients for fluid flow over a flat plate. Answer: To determine the average friction and heat transfer coefficients for fluid flow over a flat plate, follow these six steps: 1. Understand the Boundary Layer Concept: The boundary layer is the region near the plate's surface where fluid velocity changes rapidly from zero at the surface to the free stream velocity away from the plate. It can be either laminar or turbulent, depending on the Reynolds number. 2. Calculate the Reynolds Number: The Reynolds number (Re) is a dimensionless parameter that helps to determine the flow regime. Use the formula \(\operatorname{Re} = \frac{\rho U L}{\mu}\) to calculate it. 3. Determine the Local Friction Coefficient: Use the appropriate formula for laminar (Blasius equation) or turbulent (Prandtl-Karmen equation) flow regimes. 4. Calculate the Average Friction Coefficient: Integrate the local friction coefficient from the leading edge to the trailing edge of the plate and divide by the plate length. 5. Determine the Nusselt Number: The Nusselt number is a dimensionless parameter that relates the heat transfer coefficient and the fluid's thermal conductivity. Use suitable correlations based on Reynolds and Prandtl numbers and boundary layer flow regime. 6. Calculate the Average Heat Transfer Coefficient: Use the Nusselt number along with the fluid's thermal conductivity and the plate length with the formula \(h_{avg} = \frac{k}{L} \times \overline{Nu}\).

Step by step solution

01

Understand the Boundary Layer Concept

The concept of the boundary layer is important in understanding fluid flow over a flat plate. The boundary layer is the region near the surface of the plate where the fluid velocity changes rapidly from zero at the surface to the free stream velocity away from the plate. The boundary layer can be either laminar or turbulent, depending on the Reynolds number.
02

Calculate the Reynolds Number

The Reynolds number is a dimensionless parameter that helps to determine the flow regime (laminar or turbulent) of the fluid flow. The Reynolds number (Re) in the case of flow over a flat plate can be calculated using the following formula: \[\operatorname{Re} = \frac{\rho U L}{\mu}\] where ρ is the fluid density, U is the free stream velocity, L is the length of the plate, and μ is the fluid dynamic viscosity. If Re is less than 5×10^5, the flow is considered to be laminar. If Re is greater than this value, it is considered to be turbulent.
03

Determine the Local Friction Coefficient

Once the flow regime is known, we can calculate the local friction coefficient (Cf) using appropriate formulas for laminar and turbulent flows. For laminar flow, the Blasius equation is used: \[C_{f} = 0.664 \times Re^{-1 / 2}\] For turbulent flow, the Prandtl-Karmen equation is used: \[C_{f} = 0.0594 \times Re^{-1 / 5}\] Here, Re represents Reynolds number based on the distance x from the leading edge of the plate.
04

Calculate the Average Friction Coefficient

To find the average friction coefficient (Cf_avg) for the entire flat plate, integrate the local friction coefficient from the leading edge to the trailing edge of the plate and divide by the plate length. For laminar flow, the average Blasius friction coefficient is given by: \[\overline{C}_{f} = \frac{2}{L} \int_{0}^{L} C_{f} d x = \frac{1.328}{\sqrt{Re_L}}\] For turbulent flow, the average Prandtl-Karmen friction coefficient can be determined by solving the integral for the appropriate range of Reynolds number.
05

Determine the Nusselt Number

The Nusselt number is a dimensionless parameter that relates the heat transfer coefficient and the thermal conductivity of the fluid. For flow over a flat plate, different correlations can be used to find the Nusselt number based on the Reynolds and Prandtl numbers, as well as the boundary layer flow regime (laminar or turbulent). Some common correlations include Sieder-Tate, Gnielinski, and Colburn Analogies.
06

Calculate the Average Heat Transfer Coefficient

Finally, to calculate the average heat transfer coefficient (h_avg), use the Nusselt number along with the fluid's thermal conductivity (k) and the length of the plate (L) with the following formula: \[h_{avg} = \frac{k}{L} \times \overline{Nu}\] Where, \(\overline{Nu}\) is the average Nusselt number. So, applying these six steps, one can determine the average friction and heat transfer coefficients for fluid flow over a flat plate.

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

Consider a hot automotive engine, which can be approximated as a \(0.5-\mathrm{m}\)-high, \(0.40\)-m-wide, and \(0.8\)-m-long rectangular block. The bottom surface of the block is at a temperature of \(100^{\circ} \mathrm{C}\) and has an emissivity of \(0.95\). The ambient air is at $20^{\circ} \mathrm{C}\(, and the road surface is at \)25^{\circ} \mathrm{C}$. Determine the rate of heat transfer from the bottom surface of the engine block by convection and radiation as the car travels at a velocity of $80 \mathrm{~km} / \mathrm{h}$. Assume the flow to be turbulent over the entire surface because of the constant agitation of the engine block.

Engine oil at \(85^{\circ} \mathrm{C}\) flows over a \(10-\mathrm{m}\)-long flat plate whose temperature is \(35^{\circ} \mathrm{C}\) with a velocity of $2.5 \mathrm{~m} / \mathrm{s}$. Determine the total drag force and the rate of heat transfer over the entire plate per unit width.

An incandescent lightbulb is an inexpensive but highly inefficient device that converts electrical energy into light. It converts about 10 percent of the electrical energy it consumes into light while converting the remaining 90 percent into heat. (A fluorescent lightbulb will give the same amount of light while consuming only one-fourth of the electrical energy, and it will last 10 times longer than an incandescent lightbulb.) The glass bulb of the lamp heats up very quickly as a result of absorbing all that heat and dissipating it to the surroundings by convection and radiation. Consider a 10 -cm-diameter, 100 -W lightbulb cooled by a fan that blows air at \(30^{\circ} \mathrm{C}\) to the bulb at a velocity of $2 \mathrm{~m} / \mathrm{s}\(. The surrounding surfaces are also at \)30^{\circ} \mathrm{C}$, and the emissivity of the glass is \(0.9\). Assuming 10 percent of the energy passes through the glass bulb as light with negligible absorption and the rest of the energy is absorbed and dissipated by the bulb itself, determine the equilibrium temperature of the glass bulb. Assume a surface temperature of \(100^{\circ} \mathrm{C}\) for evaluation of \(\mu_{x}\). Is this a good assumption?

An automotive engine can be approximated as a \(0.4\)-m-high, \(0.60\)-m-wide, and \(0.7-\mathrm{m}\)-long rectangular block. The bottom surface of the block is at a temperature of \(75^{\circ} \mathrm{C}\) and has an emissivity of \(0.92\). The ambient air is at \(5^{\circ} \mathrm{C}\), and the road surface is at \(10^{\circ} \mathrm{C}\). Determine the rate of heat transfer from the bottom surface of the engine block by convection and radiation as the car travels at a velocity of \(60 \mathrm{~km} / \mathrm{h}\). Assume the flow to be turbulent over the entire surface because of the constant agitation of the engine block. How will the heat transfer be affected when a 2 -mm-thick layer of gunk $(k=3 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})$ has formed at the bottom surface as a result of the dirt and oil collected at that surface over time? Assume the metal temperature under the gunk is still \(75^{\circ} \mathrm{C}\).

A transformer that is \(10-\mathrm{cm}\) long, \(6.2 \mathrm{-cm}\) wide, and \(5-\mathrm{cm}\) high is to be cooled by attaching a $10-\mathrm{cm} \times 6.2-\mathrm{cm}\(-wide polished aluminum heat sink (emissivity \)=0.03$ ) to its top surface. The heat sink has seven fins, which are \(5-\mathrm{mm}\) high, 2 -mm thick, and 10 -cm long. A fan blows air at \(25^{\circ} \mathrm{C}\) parallel to the passages between the fins. The heat sink is to dissipate $12 \mathrm{~W}$ of heat, and the base temperature of the heat sink is not to exceed \(60^{\circ} \mathrm{C}\). Assuming the fins and the base plate to be nearly isothermal and the radiation heat transfer to be negligible, determine the minimum free-stream velocity the fan needs to supply to avoid overheating. Assume the flow is laminar over the entire finned surface of the transformer.

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