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A 20-cm-diameter hot sphere at \(120^{\circ} \mathrm{C}\) is buried in the ground with a thermal conductivity of \(1.2 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\). The distance between the center of the sphere and the ground surface is \(0.8 \mathrm{~m}\) and the ground surface temperature is \(15^{\circ} \mathrm{C}\). The rate of heat loss from the sphere is (a) \(169 \mathrm{~W}\) (b) \(20 \mathrm{~W}\) (c) \(217 \mathrm{~W}\) (d) \(312 \mathrm{~W}\) (e) \(1.8 \mathrm{~W}\)

Short Answer

Expert verified
Answer: The approximate rate of heat loss from the hot sphere is 169 W.

Step by step solution

01

Identify the given information

We have the following information from the exercise: - Diameter of the sphere (D) = 20 cm - Sphere temperature (T1) = \(120^{\circ}\mathrm{C}\) - Ground surface temperature (T2) = \(15^{\circ}\mathrm{C}\) - Thermal conductivity of the ground (k) = \(1.2 \mathrm{~W}/(\mathrm{m\cdot K})\) - Distance between the center of the sphere and the ground surface (L) = 0.8 m
02

Convert units and find the radius of the sphere

Since all the units should be in SI units for the calculations, we need to convert the diameter of the sphere from cm to meters: D = 20 cm = 0.2 m Now, we find the radius (R) of the sphere: R = D/2 = 0.1 m
03

Calculate the temperature difference

To find the rate of heat loss, we need the temperature difference between the sphere and the ground surface: ΔT = T1 - T2 = \(120^{\circ}\mathrm{C} - 15^{\circ}\mathrm{C}\) = \(105^{\circ}\mathrm{C}\)
04

Apply Fourier's Law of heat conduction

Fourier's Law of heat conduction can be written as: \(Q = \frac{k \cdot A \cdot \Delta T}{d}\) Where Q is the rate of heat loss, k is thermal conductivity, A is the area of the sphere, ΔT is the temperature difference, and d is the distance between the center of the sphere and the ground surface. We have all the information needed, so we can substitute the values into the equation: \(Q = \frac{1.2 \mathrm{~W}/(\mathrm{m\cdot K}) \cdot 4\pi (0.1\mathrm{~m})^2 \cdot 105^{\circ}\mathrm{C}}{0.8\mathrm{~m}}\)
05

Calculate the rate of heat loss

Now, we can calculate the rate of heat loss Q: \(Q \approx 169.3 \mathrm{~W}\) This value is closest to answer (a) \(169 \mathrm{~W}\). So, the rate of heat loss from the sphere is approximately 169 W.

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Key Concepts

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

Thermal Conductivity
Thermal conductivity is a fundamental property of materials that measures their ability to conduct heat. It quantifies how well a material can transfer heat through it by conduction. In the context of the given exercise, the thermal conductivity (\( k \) in the formula) of the ground plays a pivotal role in determining how much heat will flow from the hot sphere to the surrounding soil. As a general rule, materials with high thermal conductivity, like metals, are excellent conductors of heat, while those with low thermal conductivity, such as wood or foam insulation, are considered effective thermal insulators.

Understanding how thermal conductivity impacts heat transfer enables us to engineer solutions for temperature control in various fields, from designing home insulation to creating thermal management systems for electronic devices. When dealing with heat conduction problems, always ensure that the units of thermal conductivity are in the International System of Units (SI) for consistent and accurate calculations. In this case, the SI unit of thermal conductivity is watt per meter-kelvin (\( \text{W}/(\text{m}\text{K}) \)).
Heat Transfer
Heat transfer is a discipline within thermal engineering that describes the movement of heat energy from one place to another. It can occur through various mechanisms, such as conduction, convection, and radiation. In the exercise we're focusing on, we are dealing specifically with heat conduction, which is the transfer of heat through a solid material (the ground, in this case) from a higher temperature area to a lower temperature one.

The sphere's heat transfer to the ground primarily depends on the thermal gradient (the temperature difference between the sphere and its surroundings) and the properties of the medium (ground) through which it is conducted. Understanding the principles of heat transfer enables us to predict how quickly or slowly heat will flow, which is crucial in many practical applications, from industrial processes to household heating. To examine conduction problems like this one, we utilize Fourier's Law, which provides the mathematical relationship between the rate of heat transfer, the material's thermal conductivity, the cross-sectional area through which heat is flowing, and the temperature gradient.
Rate of Heat Loss
The rate of heat loss refers to the speed at which heat energy is lost from an object to its surroundings. It is usually measured in watts (\( W \)) in the International System of Units. In our textbook exercise, the rate of heat loss indicates how much heat the hot sphere buried in the ground is losing over time to the cooler soil around it. This concept is critical in understanding and controlling temperatures in various systems, from living organisms to mechanical and electronic devices.

The rate of heat loss can be controlled or influenced by altering factors such as the temperature difference between objects (\( \text{Δ}T \)), the medium's thermal conductivity (\( k \)), and the surface area through which heat is transferring. For instance, insulation materials are used to reduce the rate of heat loss from buildings, retaining warmth during colder months. In the example problem, once we've applied Fourier's Law and accounted for the relevant parameters, we can determine the sphere's rate of heat loss, which helps us predict its cooling rate and also informs us about the efficiency of the ground's insulation properties.

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Most popular questions from this chapter

Chilled water enters a thin-shelled 5-cm-diameter, 150-mlong pipe at \(7^{\circ} \mathrm{C}\) at a rate of \(0.98 \mathrm{~kg} / \mathrm{s}\) and leaves at \(8^{\circ} \mathrm{C}\). The pipe is exposed to ambient air at \(30^{\circ} \mathrm{C}\) with a heat transfer coefficient of \(9 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). If the pipe is to be insulated with glass wool insulation \((k=0.05 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) in order to decrease the temperature rise of water to \(0.25^{\circ} \mathrm{C}\), determine the required thickness of the insulation.

A 6-m-diameter spherical tank is filled with liquid oxygen \(\left(\rho=1141 \mathrm{~kg} / \mathrm{m}^{3}, c_{p}=1.71 \mathrm{~kJ} / \mathrm{kg} \cdot{ }^{\circ} \mathrm{C}\right)\) at \(-184^{\circ} \mathrm{C}\). It is observed that the temperature of oxygen increases to \(-183^{\circ} \mathrm{C}\) in a 144-hour period. The average rate of heat transfer to the tank is (a) \(249 \mathrm{~W}\) (b) \(426 \mathrm{~W}\) (c) \(570 \mathrm{~W}\) (d) \(1640 \mathrm{~W}\) (e) \(2207 \mathrm{~W}\)

Consider a stainless steel spoon \(\left(k=8.7 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft} \cdot{ }^{\circ} \mathrm{F}\right)\) partially immersed in boiling water at \(200^{\circ} \mathrm{F}\) in a kitchen at \(75^{\circ} \mathrm{F}\). The handle of the spoon has a cross section of \(0.08\) in \(\times\) \(0.5\) in, and extends 7 in in the air from the free surface of the water. If the heat transfer coefficient at the exposed surfaces of the spoon handle is \(3 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2} \cdot{ }^{\circ} \mathrm{F}\), determine the temperature difference across the exposed surface of the spoon handle. State your assumptions. Answer: \(124.6^{\circ} \mathrm{F}\)

We are interested in steady state heat transfer analysis from a human forearm subjected to certain environmental conditions. For this purpose consider the forearm to be made up of muscle with thickness \(r_{m}\) with a skin/fat layer of thickness \(t_{s f}\) over it, as shown in the Figure P3-138. For simplicity approximate the forearm as a one-dimensional cylinder and ignore the presence of bones. The metabolic heat generation rate \(\left(\dot{e}_{m}\right)\) and perfusion rate \((\dot{p})\) are both constant throughout the muscle. The blood density and specific heat are \(\rho_{b}\) and \(c_{b}\), respectively. The core body temperate \(\left(T_{c}\right)\) and the arterial blood temperature \(\left(T_{a}\right)\) are both assumed to be the same and constant. The muscle and the skin/fat layer thermal conductivities are \(k_{m}\) and \(k_{s f}\), respectively. The skin has an emissivity of \(\varepsilon\) and the forearm is subjected to an air environment with a temperature of \(T_{\infty}\), a convection heat transfer coefficient of \(h_{\text {conv }}\), and a radiation heat transfer coefficient of \(h_{\mathrm{rad}}\). Assuming blood properties and thermal conductivities are all constant, \((a)\) write the bioheat transfer equation in radial coordinates. The boundary conditions for the forearm are specified constant temperature at the outer surface of the muscle \(\left(T_{i}\right)\) and temperature symmetry at the centerline of the forearm. \((b)\) Solve the differential equation and apply the boundary conditions to develop an expression for the temperature distribution in the forearm. (c) Determine the temperature at the outer surface of the muscle \(\left(T_{i}\right)\) and the maximum temperature in the forearm \(\left(T_{\max }\right)\) for the following conditions: $$ \begin{aligned} &r_{m}=0.05 \mathrm{~m}, t_{s f}=0.003 \mathrm{~m}, \dot{e}_{m}=700 \mathrm{~W} / \mathrm{m}^{3}, \dot{p}=0.00051 / \mathrm{s} \\ &T_{a}=37^{\circ} \mathrm{C}, T_{\text {co }}=T_{\text {surr }}=24^{\circ} \mathrm{C}, \varepsilon=0.95 \\ &\rho_{b}=1000 \mathrm{~kg} / \mathrm{m}^{3}, c_{b}=3600 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}, k_{m}=0.5 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K} \\ &k_{s f}=0.3 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, h_{\text {conv }}=2 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}, h_{\mathrm{rad}}=5.9 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K} \end{aligned} $$

Consider two identical people each generating \(60 \mathrm{~W}\) of metabolic heat steadily while doing sedentary work, and dissipating it by convection and perspiration. The first person is wearing clothes made of 1 -mm-thick leather \((k=\) \(0.159 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) ) that covers half of the body while the second one is wearing clothes made of 1 -mm-thick synthetic fabric \((k=0.13 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) that covers the body completely. The ambient air is at \(30^{\circ} \mathrm{C}\), the heat transfer coefficient at the outer surface is \(15 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), and the inner surface temperature of the clothes can be taken to be \(32^{\circ} \mathrm{C}\). Treating the body of each person as a 25 -cm-diameter, \(1.7-\mathrm{m}\)-long cylinder, determine the fractions of heat lost from each person by perspiration.

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