/*! 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 41 A thin clectrical heater is inse... [FREE SOLUTION] | 91Ó°ÊÓ

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A thin clectrical heater is inserted between a long circular rod and a concentric tube with inner and outer radii of 20 and \(40 \mathrm{~mm}\). The rod (A) has a thermal conductivity of \(k_{A}=0.15 \mathrm{~W} / \mathrm{m}+\mathrm{K}\). while the tube (B) has a thermal conductivity of \(k_{\mathrm{B}}=1.5 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) and its cuter surface is subjected to convection with a fluid of temperature \(T_{w}=-15^{\circ} \mathrm{C}\) and heat transfer coefficient \(50 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The thermal contact resistance betueen the cylinder surfaces and the heater is negligible. (a) Determine the electrical power per unit length of the cylinders (W/m) that is required to maintain the outer surface of eylinder \(\mathrm{B}\) at \(5^{\circ} \mathrm{C}\). (b) What is the temperature at the center of cylinder A?

Short Answer

Expert verified
(a) Electrical power required is 114.7 W/m. (b) Temperature at the center of cylinder A is -9°C.

Step by step solution

01

Understand the Problem Statement

We are given a conduction and convection heat transfer problem with two concentric cylinders, A and B. We're tasked with finding the electrical power needed to maintain the temperature of the outer surface of cylinder B at 5°C and the temperature at the center of cylinder A.
02

Set Up the Heat Transfer Equations

First, we will look at the thermal resistances involved in the system. The radial heat conduction through the cylinders can be modeled using Fourier's Law in cylindrical coordinates. The convection resistance is related to the heat transfer to the surrounding fluid. The electric heater adds power, compensating for these heat losses.
03

Calculate Resistance for Conduction Through Cylinder A

The heat conducts radially through cylinder A from its inside surface to the heater. The conduction resistance for a hollow cylinder is given by:\[ R_{cond,A} = \frac{\ln(r_{h}/r_{i})}{2\pi k_{A} L} \]where \( r_{i} = 0 \) (the center) and \( r_{h} = 0.02 \text{ m} \).
04

Calculate Resistance for Conduction Through Cylinder B

Similarly, the resistance for conduction through cylinder B is:\[ R_{cond,B} = \frac{\ln(r_{o}/r_{h})}{2\pi k_{B} L} \]where \( r_{o} = 0.04 \text{ m} \) is the outer radius, and \( r_{h} = 0.02 \text{ m} \) is the heater location.
05

Calculate Resistance for Convection from Cylinder B

The resistance to convection from the outer surface of cylinder B to the fluid is:\[ R_{conv} = \frac{1}{h A} \]where \( A = 2\pi r_{o} L \) is the surface area for convection, and \( h \) is the convection coefficient.
06

Formulate the Total Heat Transfer Equation

The overall heat transfer rate (or power input per unit length) is given by combining all resistance equations under the same temperature difference:\[ q = \frac{T_{o} - T_{\infty}}{R_{total}} \]Where \( R_{total} = R_{cond,A} + R_{cond,B} + R_{conv} \). Substituting known values will allow us to solve for the power \( q \).
07

Calculate the Electrical Power Needed

Plug in all the necessary values into the formula, solve each thermal resistance, sum them up to get \( R_{total} \), and find \( q \). This calculates the power required to maintain the outer temperature of cylinder B at 5°C.
08

Determine the Temperature at the Center of Cylinder A

Now, apply the radial heat conduction formula to find the temperature gradient across cylinder A and estimate the temperature at the center, using:\[ T_{center} = T_{o} - q \cdot R_{cond,A} \]

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Key Concepts

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

Conduction
Conduction is a common form of heat transfer and occurs when heat moves through a solid material. It happens due to the collision and vibration of molecules. In our exercise, heat conduction takes place radially through two concentric cylinders, denoted as cylinder A and cylinder B.

The key to understanding conduction is to recognize the role of thermal conductivity, which measures a material's ability to conduct heat. Cylinder A has a lower thermal conductivity of 0.15 W/m·K, meaning it is less efficient in transferring heat, compared to cylinder B which has a higher thermal conductivity of 1.5 W/m·K.

Radial conduction can be analyzed using Fourier's Law, which is expressed in cylindrical coordinates for hollow cylinders. The formula is:
\[ R_{cond,A} = \frac{\ln(r_{h}/r_{i})}{2\pi k_{A} L} \]
This equation allows us to calculate the conduction resistance of cylinder A. The term \( r_h \) represents the heater location radius, while \( r_i \) is the inner radius, which is often the center of the cylinder in these types of problems.
Convection
Convection is another form of heat transfer, distinct from conduction as it involves fluid motion. It occurs adjacent to a surface where fluid, like air or water, carries heat away. In the context of our exercise, convection happens on the outer surface of cylinder B, transferring heat to the surrounding fluid of lower temperature.

The rate of heat transfer through convection depends on the heat transfer coefficient, denoted as \( h \). For cylinder B, this coefficient is given as 50 W/m²·K. The area involved in heat transfer is crucial and is calculated using the equation:
\[ A = 2\pi r_{o} L \]
where \( r_o \) is the outer radius of cylinder B. The resistance to heat transfer through convection is then calculated using:
\[ R_{conv} = \frac{1}{h A} \]
This equation helps identify how much resistance the convection offers against the heat flow, indicating its efficiency in removing heat from the cylinder.
Thermal Resistance
Thermal resistance is a crucial concept that ties together both conduction and convection in our heat transfer problem. It represents how much a material resists the flow of heat and is an essential component when calculating the heat transfer rate.

In scenarios involving multiple layers or types of heat transfer, such as in our concentric cylinders with both conduction and convection, we need to consider the total thermal resistance. This total resistance is a sum of individual resistances encountered across each medium and is calculated as:
\[ R_{total} = R_{cond,A} + R_{cond,B} + R_{conv} \]
The power needed to maintain a desired temperature difference is dictated by this total resistance. Using the equation:
\[ q = \frac{T_{o} - T_{\infty}}{R_{total}} \]
we find the overall heat transfer rate, or power per unit length. Here, \( T_o \) is the outer surface temperature, and \( T_{\infty} \) is the ambient fluid’s temperature. By knowing the total resistance, students can determine the necessary electrical power input required to maintain cylinder B’s outer surface at 5°C even when outer conditions are much colder.

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Most popular questions from this chapter

Stearn at a temperature of \(250^{\circ} \mathrm{C}\) flows through a steel pipe (AISI 1010) of 60-mm inside diameter and 75-mm autside diameter. The convection coefficient between the team and the inner surface of the pipe is \(500 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), while that between the outer surface of the pipe and the wrroundings is \(25 \mathrm{~W} / \mathrm{m}^{2}+\mathrm{K}\), The pipe emissivity is \(0.8\). and the temperature of the air and the surroundings is 20 C. What is the heat loss per unit length of pipe?

The energy transferred from the anterior chamber of the eye through the cornea varies considerably depending on whether a contact lens is worm. Treat the eye as a splerical system and assume the system to be at steady state. The convection coefficient \(h_{e}\) is unchanged with and without the contact lens in place. The cornea and the lens cover one-third of the spherical surface area. Values of the parameters representing this situation are as follows: \(\begin{array}{ll}r_{1}=10.2 \mathrm{~mm} & r_{2}=12.7 \mathrm{~mm} \\\ r_{3}=16.5 \mathrm{~mm} & T_{-a}=21^{\circ} \mathrm{C} \\ T_{s 1}=37^{\circ} \mathrm{C} & k_{2}=0.80 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K} \\\ k_{1}=0.35 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K} & h_{n}=6 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K} \\ h_{4}=12 \mathrm{~W} / \mathrm{m}^{2}-\mathrm{K} & \end{array}\) (a) Construct the thermal circuits, labeling all potentials and flows for the systems excluding the contact lens and including the contact lens. Write resistance elements in terms of appropriate parameters. (b) Determine the heat loss from the anterior chamber with and without the contact lens in place. (c) Discuss the implication of your results.

A hollow aluminem sphere, with an clectrical heater in the center, is used in tests to determine the thermal conductivity of insulating materials. The inner and outer radii of the sphere are \(0.15\) and \(0.18 \mathrm{~m}\), respectively. and testing is done under steady-state conditions with the inner surface of the aluminum maintained at \(250^{\circ} \mathrm{C}\). In a particular test, a spherical shell of insulation is cast on the outer surface of the sphere to a thickness of \(0.12 \mathrm{~m}\). The system is in a roorn for which the air temperature is \(20^{\circ} \mathrm{C}\) and the convection cocfficient at the outer surface of the insulation is \(30 \mathrm{~W} / \mathrm{m}^{2}+\mathrm{K}\). If \(80 \mathrm{~W}\) are dissipated by the heater under steady-state conditions, what is the thermal conductivity of the insulation?

The evaporator section of a refrigeration unit consists of thin-walled, 10-mm- diameter tubes through which refrigcrant passes at a temperature of \(-18^{\circ} \mathrm{C}\). Air is cooled as it flows over the tubes, maintaining a surface convection coefficient of \(100 \mathrm{~W} / \mathrm{m}^{2}\) - \(\mathrm{K}\), and is subsequently routed to the refrigerator compartment. (a) For the foregoing conditions and an air temperature of \(-3^{\circ} \mathrm{C}\), what is the rate at which heat is extracted from the air per unit tube length? (b) If the refrigerator's defrost unit malfunctions, frost will slowly accumulate on the outer tube surface. Assess the effect of frost formation on the cooling capacity of a tube for frost laycr thicknesses in the range \(0 \leq \delta \leq 4 \mathrm{~mm}\). Frost may be assumed to have a thermal conductivity of \(0.4 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\). (c) The refrigerator is disconnected after the defrost unit malfunctions and a \(2 \mathrm{~mm}\)-thick layer of frost has formed. If the tubes are in ambient air for which \(T_{\mathrm{w}}=20^{\circ} \mathrm{C}\) and natural convection maintains a convection coefficient of \(2 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), how long will it take for the frost to melt? The frost may be assamed to have a mass density of \(700 \mathrm{~kg} / \mathrm{m}^{3}\) and a later heat of fusion of \(334 \mathrm{~kJ} / \mathrm{kg}\).

An air heater may be fabricated by coiling Nichfome wire and passing air in cross flow over the wire. Consider a heater fabricated from wire of diameter \(D=\) \(1 \mathrm{~mm}\), electrical resistivity \(p_{e}=10^{-6} \mathrm{n} \cdot \mathrm{m}\), thernal conductivity \(k=25 \mathrm{~W} / \mathrm{m}=\mathrm{K}\), and emissivity \(\varepsilon=0.2\). The heater is designed to deliver air at a temperatiue of \(T_{m}=50^{\circ} \mathrm{C}\) under flow conditions that provide a convection coefficient of \(h=250 \mathrm{~W} / \mathrm{m}^{2}\). \(\mathrm{K}\) for the wire. The temperature of the housing that encloses the wire and through which the air flows is \(T_{\text {er }}=50^{\circ} \mathrm{C}\). If the maximum allowable temperature of the wire is \(T_{\max }=1200^{\circ} \mathrm{C}\), what is the maximum allowable clextric current \(n\) ? If the maximum available voltage is \(\Delta E=110 \mathrm{~V}\), what is the corresponding length \(L\) of wire that may be used in the heater and the power raing of the heater? Himt: In your solution, assume negligible temperature variations within the wire, but after obtaining the desired results, assess the validity of this arsumption.

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