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Write down the expressions for the physical laws that govern each mode of heat transfer, and identify the variables involved in each relation.

Short Answer

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Question: Identify the three modes of heat transfer and write expressions for each mode with the involved variables. Answer: The three modes of heat transfer are conduction, convection, and radiation. Their respective expressions are: 1. Conduction: \(Q = -kA\frac{\Delta T}{d}t\) 2. Convection: \(Q = hAt\Delta T\) 3. Radiation: \(Q = \epsilon\sigma AT^4t\)

Step by step solution

01

Conduction

For conduction, the physical law that relates heat transfer (Q) over a given time period (t) is given by Fourier's Law. The formula is: \[ Q = -kA\frac{\Delta T}{d}t \] The variables in this relation are: - Q: Heat transfer (Joules) - k: Thermal conductivity of the material (W/mK) - A: Cross-sectional area (m虏) - \(\Delta T\): Temperature difference between both sides of the material (K or 掳C) - d: Thickness/distance of the material (m) - t: Time period (s)
02

Convection

For convection, the physical law that relates heat transfer (Q) over a given time period (t) is given by Newton's Law of Cooling. The formula is: \[ Q = hAt\Delta T \] The variables in this relation are: - Q: Heat transfer (Joules) - h: Convection heat transfer coefficient (W/m虏K) - A: Surface area exposed to the fluid (m虏) - \(\Delta T\): Temperature difference between the surface of the object and the surrounding fluid (K or 掳C) - t: Time period (s)
03

Radiation

For radiation, the physical law that governs heat transfer (Q) over a given time period (t) is given by Stefan-Boltzmann Law. The formula is: \[ Q = \epsilon\sigma AT^4t \] The variables in this relation are: - Q: Heat transfer (Joules) - \(\epsilon\): Emissivity of the surface (dimensionless, between 0 and 1) - \(\sigma\): Stefan-Boltzmann constant (5.67 x 10鈦烩伕 W/m虏K鈦) - A: Surface area of the object (m虏) - T: Temperature of the surface in Kelvin (K) - t: Time period (s)

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Key Concepts

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

Fourier's Law of Conduction
Understanding heat transfer is crucial to many areas of engineering and physics. A primary mode through which heat moves is conduction, which can be quantified using Fourier's Law of Conduction. This law states that the rate at which heat is transferred through a material is proportional to the negative gradient of temperatures and the area through which the heat transfers.

Mathematically, Fourier's Law is represented as \[ Q = -kA\frac{\Delta T}{d}t \], where various symbols represent the heat transfer rate (Q), the material's thermal conductivity (k), the area of conduction (A), the temperature difference (\(\Delta T\)), the thickness of the material (d), and the time period (t). Thermal conductivity is a property that indicates how well a material can conduct heat, with higher values meaning better conductivity.

The negative sign indicates that heat moves from regions of higher temperature to lower temperature, aligning with the expectation that heat flows down the temperature gradient. This basic understanding of Fourier's Law can help students solve problems relating to heat conduction through various materials.
Newton's Law of Cooling
When objects transfer heat to their surroundings via fluids, such as air or water, we describe this process with Newton's Law of Cooling. This law posits that the rate of heat loss of a body is directly proportional to the difference in temperatures between the body and its surrounding environment.

The equation \[ Q = hAt\Delta T \] serves to encapsulate this relationship, indicating the heat transfer (Q), the convection heat transfer coefficient (h), the surface area exposed to the fluid (A), the temperature difference between the object's surface and the fluid (\(\Delta T\)), and the time over which this exchange occurs (t). The convection heat transfer coefficient is crucial as it defines the efficiency of the transfer process, with higher values suggesting more efficient heat convection.

Students often encounter this law in practical scenarios such as cooling of electronics or in estimating the rate at which a pot of water cools down to room temperature.
Stefan-Boltzmann Law
Radiation is another key mechanism by which heat is transferred, especially from hot surfaces. The Stefan-Boltzmann Law makes it possible to compute the rate of heat transfer by radiation from the surface of an object. According to this law, the energy radiated per unit surface area of a black body per unit time is proportional to the fourth power of the black body's temperature.

The equation detailing this law is \[ Q = \epsilon\sigma AT^4t \], where Q signifies the heat transfer, \(\epsilon\) represents the emissivity of the surface, \(\sigma\) is the Stefan-Boltzmann constant, A is the surface area, T is the temperature, and t is the time period. Emissivity is a measure of a material's ability to emit thermal radiation compared to a perfect black body and ranges from 0 to 1.

In thermal systems design and astrophysics, the Stefan-Boltzmann Law is frequently applied to predict the radiant energy exchange and the equilibrium temperature of bodies.
Thermal Conductivity
Thermal conductivity is a property intrinsic to materials that measures their capability to conduct heat. Represented by the symbol 'k' in Fourier's Law, this property plays a significant role in calculations involving heat conduction. Materials with high thermal conductivity are efficient heat conductors, making them ideal for applications like heat sinks and cooking utensils, while poor conductors, or insulators, are used in thermal insulation.

It's important to note that thermal conductivity is dependent on the material's composition, temperature, and can vary with different environments. For example, metals typically exhibit high thermal conductivity compared to nonmetals.
Convection Heat Transfer Coefficient
The convection heat transfer coefficient, denoted as 'h' in the context of Newton's Law of Cooling, is pivotal in evaluating how effectively heat is conveyed from a solid to a fluid (like air or water) or vice versa. This coefficient reflects the convective heat transfer characteristics of the fluid and the nature of the fluid flow鈥攚hether it's laminar or turbulent.

It is influenced by factors like the fluid's thermal properties, velocity, and the surface geometry of the solid. Calculating this coefficient often requires empirical correlations or experimental data, as it's not a straightforward material property like thermal conductivity.
Emissivity
The concept of emissivity is critical when discussing heat transfer by radiation, as per the Stefan-Boltzmann Law. Emissivity is the ratio of the radiation emitted by a surface to the radiation emitted by an ideal black body at the same temperature, and it's quantified by the symbol \(\epsilon\).

This dimensionless quantity can significantly affect the rate of heat transfer for objects, especially under high-temperature conditions. Surfaces with high emissivity, like matte black finishes, are excellent radiators and are used in applications like solar collector panels and infrared heaters. Meanwhile, low-emissivity surfaces, which reflect heat instead of absorbing it, are used to improve the energy efficiency of building materials.

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Most popular questions from this chapter

A 2.1-m-long, 0.2-cm-diameter electrical wire extends across a room that is maintained at \(20^{\circ} \mathrm{C}\). Heat is generated in the wire as a result of resistance heating, and the surface temperature of the wire is measured to be \(180^{\circ} \mathrm{C}\) in steady operation. Also, the voltage drop and electric current through the wire are measured to be \(110 \mathrm{~V}\) and \(3 \mathrm{~A}\), respectively. Disregarding any heat transfer by radiation, determine the convection heat transfer coefficient for heat transfer between the outer surface of the wire and the air in the room. Answer: \(156 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\)

Water enters a pipe at \(20^{\circ} \mathrm{C}\) at a rate of \(0.50 \mathrm{~kg} / \mathrm{s}\) and is heated to \(60^{\circ} \mathrm{C}\). The rate of heat transfer to the water is (a) \(20 \mathrm{~kW}\) (b) \(42 \mathrm{~kW}\) (c) \(84 \mathrm{~kW}\) (d) \(126 \mathrm{~kW}\) (e) \(334 \mathrm{~kW}\)

What is metabolism? What is the range of metabolic rate for an average man? Why are we interested in the metabolic rate of the occupants of a building when we deal with heating and air conditioning?

Heat treatment is common in processing of semiconductor material. A 200-mm- diameter silicon wafer with thickness of \(725 \mu \mathrm{m}\) is being heat treated in a vacuum chamber by infrared heater. The surrounding walls of the chamber have a uniform temperature of \(310 \mathrm{~K}\). The infrared heater provides an incident radiation flux of \(200 \mathrm{~kW} / \mathrm{m}^{2}\) on the upper surface of the wafer, and the emissivity and absorptivity of the wafer surface are \(0.70\). Using a pyrometer, the lower surface temperature of the wafer is measured to be \(1000 \mathrm{~K}\). Assuming there is no radiation exchange between the lower surface of the wafer and the surroundings, determine the upper surface temperature of the wafer. (Note: A pyrometer is a non-contacting device that intercepts and measures thermal radiation. This device can be used to determine the temperature of an object's surface.)

An AISI 316 stainless steel spherical container is used for storing chemicals undergoing exothermic reaction that provides a uniform heat flux of \(60 \mathrm{~kW} / \mathrm{m}^{2}\) to the container's inner surface. The container has an inner diameter of \(1 \mathrm{~m}\) and a wall thickness of \(5 \mathrm{~cm}\). For safety reason to prevent thermal burn on individuals working around the container, it is necessary to keep the container's outer surface temperature below \(50^{\circ} \mathrm{C}\). If the ambient temperature is \(23^{\circ} \mathrm{C}\), determine the necessary convection heat transfer coefficient to keep the container's outer surface temperature below \(50^{\circ} \mathrm{C}\). Is the necessary convection heat transfer coefficient feasible with free convection of air? If not, discuss other option to prevent the container's outer surface temperature from causing thermal burn.

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