/*! This file is auto-generated */ .wp-block-button__link{color:#fff;background-color:#32373c;border-radius:9999px;box-shadow:none;text-decoration:none;padding:calc(.667em + 2px) calc(1.333em + 2px);font-size:1.125em}.wp-block-file__button{background:#32373c;color:#fff;text-decoration:none} Problem 4 The rear window of an automobile... [FREE SOLUTION] | 91影视

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The rear window of an automobile is defogged by attaching a thin, transparent, film-type heating element to its inner surface. By electrically heating this element, a uniform heat flux may be established at the inner surface. (a) For 4-mm-thick window glass, determine the electrical power required per unit window area to maintain an inner surface temperature of \(15^{\circ} \mathrm{C}\) when the interior air temperature and convection coefficient are \(T_{\infty, i}=25^{\circ} \mathrm{C}\) and \(h_{i}=10 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), while the exterior (ambient) air temperature and convection coefficient are \(T_{\infty, o}=\) \(-10^{\circ} \mathrm{C}\) and \(h_{o}=65 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K} .\) (b) In practice \(T_{\infty \rho \rho}\) and \(h_{o}\) vary according to weather conditions and car speed. For values of \(h_{o}=2,20\), 65 , and \(100 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), determine and plot the electrical power requirement as a function of \(T_{\infty \rho}\) for \(-30 \leq T_{\infty, o} \leq 0^{\circ} \mathrm{C}\). From your results, what can you conclude about the need for heater operation at low values of \(h_{o}\) ? How is this conclusion affected by the value of \(T_{\infty, 0}\) ? If \(h \propto V^{n}\), where \(V\) is the vehicle speed and \(n\) is a positive exponent, how does the vehicle speed affect the need for heater operation?

Short Answer

Expert verified
In this problem, we calculated the electrical power required per unit window area to maintain an inner surface temperature of the rear window of an automobile with a heating element. The heat flux is determined using Fourier's law of heat conduction and the convection equation. Electrical power required is equal to the heat flux for a unit window area. We also plotted the electrical power requirement as a function of exterior air temperature for different values of exterior convection coefficients. The results suggest that the need for heater operation increases with lower exterior convection coefficients and lower exterior air temperatures. Furthermore, if the convection coefficient is proportional to the vehicle speed, the need for heater operation will change with the speed of the vehicle.

Step by step solution

01

Set up the general equation for heat flux

The general equation for heat flux through a window can be expressed as the sum of conductive and convective heat transfer: \(q = q_{conduction} + q_{convection}\) For both the interior surface and the exterior surface, we'll have the heat transfer by convection and conduction; thus: \(q = q_{cond, int} + q_{conv, int} = q_{cond, ext} + q_{conv, ext}\)
02

Calculate the heat flux for the given conditions

Let's calculate the heat flux for part (a). We are given the temperature for the inner and outer surfaces of the glass (T_inner = 15掳C and T_outter = -10掳C), as well as the convection coefficients (h_i = 10 W/m虏路K and h_o = 65 W/m虏路K). For conductive heat transfer, Fourier's law can be expressed as: \(q_{cond} = k \frac{T_{inner} - T_{outer}}{L}\) For convective heat transfer, \(q_{conv} = h (T - T_{\infty})\) Therefore, \(q_{cond, int} + q_{conv, int} = q_{cond, ext} + q_{conv, ext}\) \(k \frac{T_{inner} - T_{outer}}{L} + h_i(T_{inner} - T_{\infty,i}) = k \frac{T_{outer} - T_{inner}}{L} + h_o(T_{\infty,o} - T_{outer})\) Given values: T_inner = 15掳C, T_outter = -10掳C, h_i = 10 W/m虏路K, h_o = 65 W/m虏路K T_{\infty,i} = 25掳C, T_{\infty,o} = -10掳C, L = 4 mm = 0.004 m Assume the conductivity of window glass, k = 1 W/m路K (this value can change depending on the type of glass being used, but for this exercise, we will use 1 W/m路K as a reasonable approximation). Calculate the heat flux, q, by solving the equation above.
03

Calculate the electrical power required per unit window area

With the heat flux determined, we can now calculate the electrical power required per unit window area for maintaining the inner surface temperature. The formula for electrical power is given by P = q 脳 A, where A represents the unit window area. In this case, since we are looking for electrical power per unit window area, the result will be the heat flux (q) itself.
04

Plotting the electrical power requirement as a function of T_{\infty,o} for different values of h_o

In part (b), we need to determine and plot the electrical power requirement as a function of T_{\infty,o} for different values of h_o: 2, 20, 65, 100 W/m虏路K, and a range of exterior air temperatures from -30掳C to 0掳C. For each value of h_o, use the same method as in Steps 2 and 3 to calculate the heat flux and the electrical power required per unit window area. Then plot the electrical power requirement as a function of T_{\infty,o}.
05

Evaluate and interpret the results

After plotting the curves for different values of h_o, analyze the results and answer the questions: 1. What can you conclude about the need for heater operation at low values of h_o? 2. How is this conclusion affected by the value of T_{\infty,o}? 3. If h 鈭 V^n, where V is the vehicle speed and n is a positive exponent, how does the vehicle speed affect the need for heater operation?

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Key Concepts

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

Conduction
Conduction is a fundamental process of heat transfer that occurs within a material or between materials in direct contact with each other. It is the transfer of heat through a material without any movement of the material itself. Conduction happens due to the transfer of kinetic energy from hotter molecules to cooler ones. In simpler terms, when you touch a warm object, you experience conduction.

Key points about conduction include:
  • It is driven by a temperature difference.
  • No mass movement occurs within the substance.
  • The rate of conduction depends on the thermal conductivity of the material.

In the context of the rear window defogger, conduction occurs through the glass, with the heat moving from the inner surface (with the heating element) to the outer surface exposed to colder outside air. Fourier's Law quantifies conduction as follows:
\[ q_{cond} = k \frac{T_{inner} - T_{outer}}{L} \]
where:
  • \( k \) is the thermal conductivity of the glass.
  • \( T_{inner} \) and \( T_{outer} \) are the temperatures at the inner and outer surfaces.
  • \( L \) is the thickness of the glass.
The more thermally conductive the material, the easier it is for heat to transfer through it via conduction.
Convection
Convection is another mode of heat transfer and occurs when heat is transferred by the movement of fluids鈥攅ither gases or liquids. In convection, the fluid motion is the primary driver for heat transfer, caused either by external forces (like a fan or a pump) or through natural buoyancy forces arising from temperature differences.

Key characteristics of convection include:
  • Involves fluid movement, enhancing heat transfer.
  • Can be classified as either natural (due to buoyancy) or forced (due to mechanical means).
  • Is a key factor in designing heating and cooling systems.
In our example of the automobile defogger, convection occurs at both the inner and outer surfaces. The interior air warms the glass through the heating element's inner surface, while the exterior air cools the outer surface. The heat transfer by convection can be represented by:
\[ q_{conv} = h(T - T_{\infty}) \]
where:
  • \( h \) represents the convection heat transfer coefficient.
  • \( T \) is the temperature of the surface.
  • \( T_{\infty} \) is the ambient temperature.
Understanding convection helps in evaluating how efficiently a surface can transfer heat to its surroundings or how fast it can cool down.
Heat Flux
Heat flux is an important concept in thermal dynamics, quantifying the rate of heat transfer per unit area. It is a vector quantity, having both a magnitude and a direction. In simpler terms, heat flux tells us how much heat is being transferred through a given area over a specific period of time.

Important aspects of heat flux are:
  • Measured in watts per square meter (\( W/m^2 \)).
  • Combines conduction and convection contributions.
  • Determines the energy transfer efficiency.
In the automobile window problem, the heat flux through the glass is a crucial factor, as it combines both the conduction through the glass material and the convection at the surfaces. It is crucial for calculating the necessary power for the defogger, as the formula for electrical power required is \( P = q \times A \), where \( A \) is the area through which heat flows.

By establishing a uniform heat flux, we ensure even heating across the surface, preventing hot or cold spots in the glass.
Thermal Conductivity
Thermal conductivity is a critical property of materials, indicating how well a material can conduct heat. Materials with high thermal conductivity quickly transfer heat, making them good conductors, while materials with low thermal conductivity are insulators. This property is integral when designing systems that need effective heat management or insulation.

Key points about thermal conductivity include:
  • Denoted as \( k \), measured in watts per meter per Kelvin (\( W/m\cdot K \)).
  • Varies depending on the material's structure and composition.
  • Plays a vital role in determining the rate of heat transfer via conduction in materials.
In the context of the automobile window, thermal conductivity (\( k \)) of the glass determines how efficiently heat flows from the heated inner surface to the colder outer surface. It is essential for calculating conduction heat flux and thereby other parameters like heat flux and electrical power required for heating. A balance is needed to ensure the glass effectively transfers enough heat to keep the surface free of fog without excessive power consumption.

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Most popular questions from this chapter

Consider a plane composite wall that is composed of two materials of thermal conductivities \(k_{\mathrm{A}}=0.1 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) and \(k_{\mathrm{B}}=0.04 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) and thicknesses \(L_{\mathrm{A}}=10 \mathrm{~mm}\) and \(L_{\mathrm{B}}=20 \mathrm{~mm}\). The contact resistance at the interface between the two materials is known to be \(0.30 \mathrm{~m}^{2} \cdot \mathrm{K} / \mathrm{W}\). Material A adjoins a fluid at \(200^{\circ} \mathrm{C}\) for which \(h=10\) \(\mathrm{W} / \mathrm{m}^{2} \cdot \mathrm{K}\), and material \(\mathrm{B}\) adjoins a fluid at \(40^{\circ} \mathrm{C}\) for which \(h=20 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). (a) What is the rate of heat transfer through a wall that is \(2 \mathrm{~m}\) high by \(2.5 \mathrm{~m}\) wide? (b) Sketch the temperature distribution.

Turbine blades mounted to a rotating disc in a gas turbine engine are exposed to a gas stream that is at \(T_{\infty}=1200^{\circ} \mathrm{C}\) and maintains a convection coefficient of \(h=250 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) over the blade. The blades, which are fabricated from Inconel, \(k \approx 20 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), have a length of \(L=50 \mathrm{~mm}\). The blade profile has a uniform cross-sectional area of \(A_{c}=6 \times 10^{-4} \mathrm{~m}^{2}\) and a perimeter of \(P=110 \mathrm{~mm}\). A proposed blade- cooling scheme, which involves routing air through the supporting disc, is able to maintain the base of each blade at a temperature of \(T_{b}=300^{\circ} \mathrm{C}\). (a) If the maximum allowable blade temperature is \(1050^{\circ} \mathrm{C}\) and the blade tip may be assumed to be adiabatic, is the proposed cooling scheme satisfactory? (b) For the proposed cooling scheme, what is the rate at which heat is transferred from each blade to the coolant?

Copper tubing is joined to a solar collector plate of thickness \(t\), and the working fluid maintains the temperature of the plate above the tubes at \(T_{o}\). There is a uniform net radiation heat flux \(q_{\text {rad }}^{\prime \prime}\) to the top surface of the plate, while the bottom surface is well insulated. The top surface is also exposed to a fluid at \(T_{\infty}\) that provides for a uniform convection coefficient \(h\). (a) Derive the differential equation that governs the temperature distribution \(T(x)\) in the plate. (b) Obtain a solution to the differential equation for appropriate boundary conditions.

Consider an extended surface of rectangular cross section with heat flow in the longitudinal direction. In this problem we seek to determine conditions for which the transverse ( \(y\)-direction) temperature difference within the extended surface is negligible compared to the temperature difference between the surface and the environment, such that the one-dimensional analysis of Section 3.6.1 is valid. (a) Assume that the transverse temperature distribution is parabolic and of the form $$ \frac{T(y)-T_{o}(x)}{T_{s}(x)-T_{o}(x)}=\left(\frac{y}{t}\right)^{2} $$ where \(T_{s}(x)\) is the surface temperature and \(T_{o}(x)\) is the centerline temperature at any \(x\)-location. Using Fourier's law, write an expression for the conduction heat flux at the surface, \(q_{y}^{\prime \prime}(t)\), in terms of \(T_{s}\) and \(T_{a^{+}}\) (b) Write an expression for the convection heat flux at the surface for the \(x\)-location. Equating the two expressions for the heat flux by conduction and convection, identify the parameter that determines the ratio \(\left(T_{o}-T_{s}\right) /\left(T_{s}-T_{\infty}\right)\). (c) From the foregoing analysis, develop a criterion for establishing the validity of the onedimensional assumption used to model an extended surface.

A long cylindrical rod of diameter \(200 \mathrm{~mm}\) with thermal conductivity of \(0.5 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) experiences uniform volumetric heat generation of \(24,000 \mathrm{~W} / \mathrm{m}^{3}\). The rod is encapsulated by a circular sleeve having an outer diameter of \(400 \mathrm{~mm}\) and a thermal conductivity of \(4 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\). The outer surface of the sleeve is exposed to cross flow of air at \(27^{\circ} \mathrm{C}\) with a convection coefficient of \(25 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). (a) Find the temperature at the interface between the rod and sleeve and on the outer surface. (b) What is the temperature at the center of the rod?

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