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How do rating problems in heat transfer differ from the sizing problems?

Short Answer

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Answer: Rating problems in heat transfer deal with determining the performance of a given heat exchanger under specified conditions, while sizing problems are concerned with designing or modifying a heat exchanger to achieve a desired performance. When solving a rating problem, the focus is on calculating output quantities based on known design parameters and boundary conditions, while solving a sizing problem involves finding the design parameters that meet specific performance criteria using trial-and-error, iteration, or optimization techniques.

Step by step solution

01

Definitions of Rating and Sizing Problems

Rating problems in heat transfer are concerned with determining the heat transfer rate, temperature distribution, or other output quantities when the geometry and boundary conditions are known. In other words, rating problems involve finding the performance of a given heat exchanger under specified conditions. On the other hand, sizing problems in heat transfer deal with determining the dimensions, geometry, or other design parameters of a heat exchanger or heat transfer system to achieve a desired performance. In this case, the boundary conditions and desired performance (e.g., heat transfer rate) are known, and the objective is to design the heat exchanger appropriately.
02

Differences in Approaches

When solving a rating problem in heat transfer, the main focus is on calculating the heat transfer rate or temperature distribution based on the given design parameters and boundary conditions. This typically involves: 1. Using the appropriate heat transfer equation or correlations, depending on the mode of heat transfer (conduction, convection, or radiation) 2. Applying the boundary conditions to the equations 3. Solving the equations to obtain the desired output quantities (e.g., heat transfer rate, temperatures at different locations) In contrast, when solving a sizing problem, the goal is to design or modify the heat exchanger to achieve the desired performance. This may involve: 1. Identifying the specific performance criteria that need to be met (e.g., heat transfer rate, pressure drop) 2. Using the appropriate heat transfer equation or correlations, along with trial-and-error, iteration, or optimization techniques, to find the design parameters that meet these criteria 3. Evaluating the design for practicality and other considerations (e.g., cost, manufacturability, safety)
03

Summary

Rating problems in heat transfer deal with determining the performance of a given heat exchanger under specified conditions, while sizing problems are concerned with designing or modifying a heat exchanger to achieve a desired performance. The approaches to solving these problems are different, with rating problems focusing on calculating the output quantities based on known design parameters and boundary conditions, and sizing problems focusing on finding the design parameters that meet specific performance criteria.

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Most popular questions from this chapter

In the metal processing industry, heat treatment of metals is commonly done using electrically heated draw batch furnaces. Consider a furnace that is situated in a room with surrounding air temperature of \(30^{\circ} \mathrm{C}\) and an average convection heat transfer coefficient of $12 \mathrm{~W} / \mathrm{m}^{2}\(. \)\mathrm{K}$. The furnace front is made of a steel plate with thickness of \(20 \mathrm{~mm}\) and a thermal conductivity of $25 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$. The outer furnace front surface has an emissivity of \(0.23\), and the inside surface is subjected to a heat flux of $8 \mathrm{~kW} / \mathrm{m}^{2}$. Determine the outside surface temperature of the furnace front.

An electronic package in the shape of a sphere with an outer diameter of $100 \mathrm{~mm}$ is placed in a large laboratory room. The surface emissivity of the package can assume three different values \((0.2,0.25\), and \(0.3)\). The walls of the room are maintained at a constant temperature of $77 \mathrm{~K}$. The electronics in this package can only operate in the surface temperature range of $40^{\circ} \mathrm{C} \leq T_{s} \leq 85^{\circ} \mathrm{C}\(. Determine the range of power dissipation \)(\dot{W})$ for the electronic package over this temperature range for the three surface emissivity values \((\varepsilon)\). Plot the results in terms of \(\dot{W}(\mathrm{~W})\) vs. \(T_{s}\left({ }^{\circ} \mathrm{C}\right)\) for the three different values of emissivity over a surface temperature range of 40 to \(85^{\circ} \mathrm{C}\) with temperature increments of \(5^{\circ} \mathrm{C}\) (total of 10 data points for each \(\varepsilon\) value). Provide a computer- generated graph for the display of your results, and tabulate the data used for the graph. Comment on the results obtained.

An electric current of 1 A passing through a cable The cable is covered with polyethylene insulation, and convection occurs at the outer surface of the insulation. The ambient temperature is \(20^{\circ} \mathrm{C}\) with a convection heat transfer coefficient of $5 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\(, and the surface area subjected to the convection is \)0.1 \mathrm{~m}^{2}$. The ASTM D1351 standard specifies that thermoplastic polyethylene insulation is suitable for use on electrical cable with operation at temperatures up to \(75^{\circ} \mathrm{C}\). Under these conditions, will the polyethylene insulation for the cable meet the ASTM D1351 standard? If the polyethylene insulation does not meet the ASTM D1351 standard, then discuss possible solutions to meet the standard.

A 2-kW electric resistance heater submerged in 30-kg water is turned on and kept on for \(10 \mathrm{~min}\). During the process, \(500 \mathrm{~kJ}\) of heat is lost from the water. The temperature rise of the water is (a) \(5.6^{\circ} \mathrm{C}\) (b) \(9.6^{\circ} \mathrm{C}\) (c) \(13.6^{\circ} \mathrm{C}\) (d) \(23.3^{\circ} \mathrm{C}\) (e) \(42.5^{\circ} \mathrm{C}\)

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