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Standard air flows over a 2 -m-long, 3 -m-wide flat surface at a speed of \(30 \mathrm{~m} / \mathrm{s}\). The boundary layer is assumed to be in the smooth turbulent regime over the entire surface, and the velocity distribution within the boundary layer is assumed to follow the one-seventh power law distribution. (a) Estimate the thickness of the boundary layer at the downstream end of the surface. (b) Compare the drag force on the front half of the surface with the drag force on the back half of the surface.

Short Answer

Expert verified
Boundary layer thickness: 0.03 m. Drag force is larger on the front half (53.6 N) than on the back half (43.2 N).

Step by step solution

01

Identify the Problem

The problem involves calculating the boundary layer thickness and comparing drag forces for smooth turbulent flow over a flat plate using the one-seventh power law for velocity distribution in the boundary layer.
02

Apply Velocity Profile for Boundary Layer

The velocity distribution in the boundary layer for turbulent flow is given by the one-seventh power law: \( \left( \frac{u}{U} \right) = \left( \frac{y}{\delta} \right)^{1/7} \), where \(u\) is the local velocity of air, \(U\) is the free stream velocity, \(y\) is the distance from the surface, and \(\delta\) is the boundary layer thickness.
03

Calculate Boundary Layer Thickness

For a turbulent boundary layer over a flat plate, the empirical formula for boundary layer thickness at the end of the plate is \( \delta = 0.37 x / Re_x^{1/5} \). First, compute the Reynolds number: \( Re_x = \frac{U x}{u} \), where \( U = 30 \ \mathrm{m/s} \), \(x = 2 \ \mathrm{m} \), and \( u = 1.5 \times 10^{-5} \ \mathrm{m^2/s} \).
04

Calculate Reynolds Number

Reynolds number, \( Re_x = \frac{30 \times 2}{1.5 \times 10^{-5}} = 4 \times 10^6 \).
05

Compute Boundary Layer Thickness

Plug in the Reynolds number to get the boundary layer thickness: \( \delta = \frac{0.37 \times 2}{(4 \times 10^6)^{1/5}} \approx 0.03 \ \mathrm{m} \).
06

Estimate Drag Force on Surface

Drag force per unit width for turbulent flow over a flat plate is \( F_d' = 0.664 \frac{\rho U^2}{2} \times \left( 1 / Re_L^{1/5} \right) \times L \), where \(L\) is length over which drag force is being calculated and \(\rho\) is air density, assumed \( 1.225 \ \mathrm{kg/m^3} \). Compute for both the front half and back half of the plate.
07

Compute Drag on Front Half

For the front half (\(L = 1 \ \mathrm{m}\)), \( Re_L = \frac{30 \times 1}{1.5 \times 10^{-5}} = 2 \times 10^6 \). Calculate drag force: \( Fd_1' = 0.664 \times \frac{1.225 \times 30^2}{2} \times \left( \frac{1}{(2 \times 10^6)^{1/5}} \right) \times 1 \approx 53.6 \ \mathrm{N} \).
08

Compute Drag on Back Half

For the back half (\(L = 1 \ \mathrm{m}\)), total \(Re_L = 4 \times 10^6 \) but drag on this segment follows similar calc. as front half, evaluated separately \(L = 1 \ \mathrm{m}\): \(F_{d2}' = 0.664 \times \frac{1.225 \times 30^2}{2} \times \left( \frac{1}{(4 \times 10^6)^{1/5}} \right) \times 1 \approx 43.2 \ \mathrm{N} \).
09

Evaluate Drag Forces Comparison

Compare the drag forces: the drag force on the front half of the surface (53.6 N) is greater than the drag force on the back half of the surface (43.2 N).

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Key Concepts

These are the key concepts you need to understand to accurately answer the question.

Boundary Layer Thickness
The boundary layer is the region of fluid flow where the effects of viscosity are significant, primarily near the surface of an object. Its thickness, denoted by \( \delta \), is a critical factor when studying fluid dynamics, particularly in the context of flow over flat surfaces.
For a turbulent boundary layer over a flat plate, an empirical formula is often used to estimate this thickness: \( \delta = 0.37 x / Re_x^{1/5} \). Here, \( x \) is the distance from the leading edge of the surface, and \( Re_x \) is the local Reynolds number. These formulas help predict how thick the layer of slowing air becomes as it spreads out along the plate.
In our exercise, understanding the boundary layer thickness assists in comprehending how resistance to flow, or drag, develops over the surface.
Reynolds Number
The Reynolds number is a dimensionless value used to predict flow patterns in different fluid flow situations. It indicates whether the flow will be laminar or turbulent and is defined by the formula: \( Re_x = \frac{U x}{u} \). Here:
  • \( U \) is the free stream velocity.
  • \( x \) is the characteristic length, such as distance from the leading edge.
  • \( u \) is the kinematic viscosity of the fluid.
The value of the Reynolds number is crucial in this exercise because it dictates the regime of flow encountered—whether the flow remains smooth or is turbulent, ultimately affecting drag force calculations. For instance, a high Reynolds number indicates turbulent flow, as seen in our example with \( Re_x = 4 \times 10^6 \). Such insights help engineers design surfaces that minimize drag by manipulating flow behaviors efficiently.
Drag Force
The drag force is the resistance force caused by the motion of a body through a fluid, like air or water. For a flat surface in turbulent flow, calculating drag force involves understanding the shear stress acting along the surface due to the fluid's viscosity.
In our context, the drag force per unit width for turbulent flow over a flat plate is determined with:
\( F_d' = 0.664 \frac{\rho U^2}{2} \times \left( 1 / Re_L^{1/5} \right) \times L \), where:
  • \( \rho \) is the density of the fluid.
  • \( U \) is the free stream velocity.
  • \( L \) is the length over which drag is being calculated.
Understanding drag force calculations is essential for minimizing energy usage and maximizing efficiency in vehicles, airplanes, and even in the design of skyscrapers to withstand wind.
Smooth Turbulent Regime
The smooth turbulent regime is a specific state of flow where turbulence is present but the surface beneath the fluid is smooth enough that roughness does not significantly affect the boundary layer. This regime typically occurs at relatively high Reynolds numbers and is modeled using theoretical laws like the one-seventh power law.
The one-seventh power law is a simplified model for velocity profiles within the boundary layer of a flat plate. According to this law, the velocity at a point within the boundary layer changes with the distance from the wall, raised to the power of 1/7: \( \left( \frac{u}{U} \right) = \left( \frac{y}{\delta} \right)^{1/7} \).
This concept helps predict how a fluid's velocity profile looks along a flat surface, offering insights into how to shape surfaces to optimize performance in engineering applications. It ensures that real-world conditions like pressure drop and drag are accurately estimated for designs in aerodynamics and hydrodynamics.

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Most popular questions from this chapter

The velocity distribution in a laminar boundary layer can be described by the following normalized quadric distribution: $$ u^{*}=2 y^{*}-2 y^{* 3}+y^{* 4} $$ where \(u^{*}=u / U, y^{*}=y / \delta, u\) is the velocity at a distance \(y\) from the surface, \(U\) is the free-stream velocity, and \(\delta\) is the thickness of the boundary layer. Determine the ratio of the displacement thickness to the boundary layer thickness.

Consider the general case of a fluid flowing over a smooth flat rectangular surface of length \(L\) and width \(b\). Show that if the boundary layer is turbulent over the entire surface and the velocity profile within the boundary layer can be described by the one-seventh power law distribution, then \(50 \%\) of the total drag force on the surface is exerted over approximately the front \(20 \%\) of the surface.

A self-similar velocity profile in the boundary layer over a flat plate is described by $$ \frac{u}{U}=\left\\{\begin{array}{ll} f\left(\frac{y}{\delta}\right), & 0 \leq \frac{y}{\delta} \leq 1 \\ 1, & \frac{y}{\delta}>1 \end{array}\right. $$ For the case where the boundary layer grows from zero thickness at \(x=0\), show that the thickness of the boundary layer, \(\delta\), as a function of the distance \(x\) from the leading edge of the plate is described by $$ \frac{\delta}{x}=\frac{C_{1}}{\operatorname{Re}_{x}^{\frac{1}{2}}} $$ where \(C_{1}\) is a constant that depends only on the functional form of the self-similar velocity distribution.

(a) What is the ratio of the momentum thickness to the boundary-layer thickness given by the Blasius solution? (b) It is sometimes assumed that the velocity distribution in the boundary layer is given by the following power- law relationship: $$ \frac{u}{U}=\left\\{\begin{array}{ll} \left(\frac{y}{\delta}\right)^{\frac{1}{n}}, & y \leq \delta \\ 1, & y>\delta \end{array}\right. $$ where \(u\) is the longitudinal speed within the boundary layer, \(U\) is the free-stream speed, \(y\) is the distance from the surface, \(\delta\) is the thickness of the boundary layer, and \(n\) is a number, usually assumed to be in the range of \(5-10 .\) What value of \(n\) will give the same ratio of momentum thickness to boundary-layer thickness as that given by the Blasius solution?

From an analysis of pipe flow data, the following empirical expression for the local wall shear stress, \(\tau_{\mathrm{w}}\), as a function of the boundary- layer thickness, \(\delta\), has been derived (by Prandtl) and is widely accepted: $$ \tau_{\mathrm{w}}=0.0233 \rho U^{2}\left(\frac{\nu}{U \delta}\right)^{\frac{1}{4}} $$ where \(\rho\) and \(\nu\) are the density and kinematic viscosity of the fluid, respectively, and \(U\) is the free-stream velocity. If the one-seventh power law velocity distribution is assumed to exist within the boundary layer, then the ratio of the momentum thickness, \(\theta,\) to the boundary-layer thickness can be shown to be given by \(\theta / \delta=7 / 72\). Show that the two given relationships yield the following equations describing var-ious properties of the boundary layer: $$ \frac{\delta}{x}=\frac{0.382}{\operatorname{Re}_{x}^{\frac{1}{5}}}, \quad \frac{\tau_{\mathrm{w}}}{\frac{1}{2} \rho U^{2}}=\frac{0.0594}{\operatorname{Re}_{x}^{\frac{1}{5}}}, \quad \frac{F_{\mathrm{D}}}{\frac{1}{2} \rho U^{2} L b}=\frac{0.0735}{\operatorname{Re}_{\mathrm{L}}^{\frac{1}{5}}} $$ where \(x\) is the distance along a flat surface of length \(L\) and width \(b\) and \(F_{\mathrm{D}}\) is the total drag force on the surface.

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