/*! 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 38 An internally reversible refrige... [FREE SOLUTION] | 91Ó°ÊÓ

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An internally reversible refrigerator has a modified coefficient of performance accounting for realistic heat transfer processes of $$ \mathrm{COP}_{m}=\frac{q_{\text {in }}}{\dot{W}}=\frac{q_{\text {in }}}{q_{\text {out }}-q_{\text {in }}}=\frac{T_{c, i}}{T_{h, i}-T_{c, i}} $$ where \(q_{\text {in }}\) is the refrigerator cooling rate, \(q_{\text {out }}\) is the heat rejection rate, and \(\dot{W}\) is the power input. Show that \(\mathrm{COP}_{m}\) can be expressed in terms of the reservoir temperatures \(T_{c}\) and \(T_{h}\), the cold and hot thermal resistances \(R_{L, c}\) and \(R_{t, h}\), and \(q_{\text {in }}\), as $$ \mathrm{COP}_{m}=\frac{T_{c}-q_{\mathrm{in}} R_{\mathrm{tot}}}{T_{h}-T_{c}+q_{\mathrm{in}} R_{\mathrm{tot}}} $$ where \(R_{\mathrm{tot}}=R_{t, c}+R_{t, h}\). Also, show that the power input may be expressed as $$ \dot{W}=q_{\mathrm{in}} \frac{T_{h}-T_{c}+q_{\mathrm{in}} R_{\mathrm{id \textrm {t }}}}{T_{c}-q_{\mathrm{in}} R_{\mathrm{tot}}} $$

Short Answer

Expert verified
In this problem, we derived the equation for the modified coefficient of performance (COP_m) as: \[ \mathrm{COP}_{m} = \frac{T_c - q_{in} R_{tot}}{T_h - T_c + q_{in} R_{tot}} \] We also found the expression for the power input \(\dot{W}\) as: \[ \dot{W} = q_{in} \frac{T_h - T_c + q_{in} R_{tot}}{T_c - q_{in} R_{tot}} \]

Step by step solution

01

Write down the given Data

We are given the equation for the modified coefficient of performance (COP_m) as: \[ \mathrm{COP}_{m}=\frac{T_{c, i}}{T_{h, i}-T_{c, i}} \] We are also given that: \[ q_{in} = T_{c, i} - R_{t, c} (T_{c, i} - T_c) \] and \[ q_{out} = T_{h, i} - R_{t, h} (T_h - T_{h, i}) \] Finally, we are given that the total resistance \(R_{tot} = R_{t, c} + R_{t, h}\).
02

Express \(T_{c, i}\) and \(T_{h, i}\) in terms of \(q_{in}\) and resistances

We can rewrite the given equations for \(q_{in}\) and \(q_{out}\) as: \[ T_{c, i} = q_{in} + R_{t, c} (T_c - q_{in}) \\ T_{h, i} = q_{out} - R_{t, h} (T_h - q_{out}) \]
03

Substitute the expressions for \(T_{c, i}\) and \(T_{h, i}\) into the COP_m equation

Substituting the expressions for \(T_{c, i}\) and \(T_{h, i}\) from step 2 into the equation for COP_m, we get: \[ \mathrm{COP}_{m}=\frac{q_{in} + R_{t, c}(T_c - q_{in})}{q_{out} - R_{t, h}(T_h - q_{out}) - (q_{in} + R_{t, c}(T_c - q_{in}))} \]
04

Simplify the expression for COP_m

Simplifying the expression for COP_m, we get: \[ \mathrm{COP}_{m} = \frac{T_c - q_{in}R_{t, c}}{T_h - T_c + q_{in} (R_{t, c} + R_{t, h})} \] Since we know \(R_{tot} = R_{t, c} + R_{t, h}\), we can plug it into the equation: \[ \mathrm{COP}_{m} = \frac{T_c - q_{in} R_{tot}}{T_h - T_c + q_{in} R_{tot}} \]
05

Find the power input \(\dot{W}\) equation

We are also asked to find an expression for the power input, which is obtained from the definition of COP as follows: \[ \mathrm{COP}_{m}=\frac{q_{in}}{\dot{W}} \Rightarrow \dot{W} = \frac{q_{in}}{\mathrm{COP}_{m}} \] Now, we can substitute the expression we derived for the COP_m in step 4: \[ \dot{W} = q_{in} \frac{T_h - T_c + q_{in} R_{tot}}{T_c - q_{in} R_{tot}} \] Now, we have derived the equation for the COP_m and the power input in terms of the given variables.

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Key Concepts

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

Thermal Resistances
In refrigeration systems, thermal resistances play a crucial role in understanding how heat is transferred through different parts of the system. Imagine thermal resistance like an obstacle that heat must overcome to move from one point to another.
  • Thermal resistance is present in both the cold and hot regions of a refrigeration system, denoted as \( R_{t, c} \) for the cold side and \( R_{t, h} \) for the hot side.
  • The total thermal resistance, \( R_{tot} \), is simply the sum of both \( R_{t, c} \) and \( R_{t, h} \). This total is important because it affects the efficiency with which the refrigeration system operates.
Thermal resistance impacts the modified coefficient of performance by altering how heat enters and exits the system. Therefore, understanding and controlling thermal resistances can lead to more efficient refrigeration cycles.
Heat Transfer Processes
The process of transferring heat is at the heart of refrigeration cycles. Heat transfer determines the cooling rate \( q_{in} \) in a refrigerator. In simple terms, heat transfer is moving heat from a cooler area to a warmer one. This reverse heat flow requires work, achieved through the refrigeration cycle.
  • Heat enters the system from the cooling load \( q_{in} \) and exits as rejected heat \( q_{out} \). These processes are governed by the laws of thermodynamics.
  • Understanding these processes involves equations that use the reservoir temperatures, \( T_c \) and \( T_h \), and modifying factors such as thermal resistances.
By optimizing heat transfer processes, the performance of the refrigeration system improves, leading to a better Coefficient of Performance, or \( \text{COP} \), which measures the efficiency of the system.
Refrigeration Cycle
The refrigeration cycle is a system's method of removing heat from a low-temperature environment and dumping it in a high-temperature environment, effectively cooling the interior space of a refrigerator. It involves repeating stages of compression, condensation, expansion, and evaporation.
  • The cycle starts with the compression of refrigerant gas, which increases its pressure and temperature.
  • Next, the hot gas flows through the condenser, where it cools and condenses into a liquid.
  • The liquid refrigerant then expands and cools as it passes through an expansion valve.
  • Finally, it absorbs heat as it evaporates in the evaporator, completing the cycle.
This cycle's efficiency is impacted by the modified coefficient of performance, which can be calculated using temperatures, thermal resistances, and heat transfer rates. By understanding and correctly manipulating these variables, a refrigeration system's efficiency can be significantly enhanced.

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Most popular questions from this chapter

An electric resistance heater is embedded in a long cylinder of diameter \(30 \mathrm{~mm}\). When water with a temperature of \(25^{\circ} \mathrm{C}\) and velocity of \(1 \mathrm{~m} / \mathrm{s}\) flows crosswise over the cylinder, the power per unit length required to maintain the surface at a uniform temperature of \(90^{\circ} \mathrm{C}\) is \(28 \mathrm{~kW} / \mathrm{m}\). When air, also at \(25^{\circ} \mathrm{C}\), but with a velocity of \(10 \mathrm{~m} / \mathrm{s}\) is flowing, the power per unit length required to maintain the same surface temperature is \(400 \mathrm{~W} / \mathrm{m}\). Calculate and compare the convection coefficients for the flows of water and air.

A thin electrical heating element provides a uniform heat flux \(q_{o}^{\prime \prime}\) to the outer surface of a duct through which airflows. The duct wall has a thickness of \(10 \mathrm{~mm}\) and a thermal conductivity of \(20 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\). (a) At a particular location, the air temperature is \(30^{\circ} \mathrm{C}\) and the convection heat transfer coefficient between the air and inner surface of the duct is \(100 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). What heat flux \(q_{o}^{\prime \prime}\) is required to maintain the inner surface of the duct at \(T_{i}=85^{\circ} \mathrm{C}\) ? (b) For the conditions of part (a), what is the temperature \(\left(T_{o}\right)\) of the duct surface next to the heater? (c) With \(T_{i}=85^{\circ} \mathrm{C}\), compute and plot \(q_{o}^{\prime \prime}\) and \(T_{o}\) as a function of the air-side convection coefficient \(h\) for the range \(10 \leq h \leq 200 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Briefly discuss your results.

A small sphere of reference-grade iron with a specific heat of \(447 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\) and a mass of \(0.515 \mathrm{~kg}\) is suddenly immersed in a water-ice mixture. Fine thermocouple wires suspend the sphere, and the temperature is observed to change from 15 to \(14^{\circ} \mathrm{C}\) in \(6.35 \mathrm{~s}\). The experiment is repeated with a metallic sphere of the same diameter, but of unknown composition with a mass of \(1.263 \mathrm{~kg}\). If the same observed temperature change occurs in \(4.59 \mathrm{~s}\), what is the specific heat of the unknown material?

Consider a surface-mount type transistor on a circuit board whose temperature is maintained at \(35^{\circ} \mathrm{C}\). Air at \(20^{\circ} \mathrm{C}\) flows over the upper surface of dimensions \(4 \mathrm{~mm} \times\) \(8 \mathrm{~mm}\) with a convection coefficient of \(50 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Three wire leads, each of cross section \(1 \mathrm{~mm} \times 0.25 \mathrm{~mm}\) and length \(4 \mathrm{~mm}\), conduct heat from the case to the circuit board. The gap between the case and the board is \(0.2 \mathrm{~mm}\). (a) Assuming the case is isothermal and neglecting radiation, estimate the case temperature when \(150 \mathrm{~mW}\) is dissipated by the transistor and (i) stagnant air or (ii) a conductive paste fills the gap. The thermal conductivities of the wire leads, air, and conductive paste are \(25,0.0263\), and \(0.12 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), respectively. (b) Using the conductive paste to fill the gap, we wish to determine the extent to which increased heat dissipation may be accommodated, subject to the constraint that the case temperature not exceed \(40^{\circ} \mathrm{C}\). Options include increasing the air speed to achieve a larger convection coefficient \(h\) and/or changing the lead wire material to one of larger thermal conductivity. Independently considering leads fabricated from materials with thermal conductivities of 200 and \(400 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), compute and plot the maximum allowable heat dissipation for variations in \(h\) over the range \(50 \leq h \leq 250 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\).

An overhead 25-m-long, uninsulated industrial steam pipe of \(100-\mathrm{mm}\) diameter is routed through a building whose walls and air are at \(25^{\circ} \mathrm{C}\). Pressurized steam maintains a pipe surface temperature of \(150^{\circ} \mathrm{C}\), and the coefficient associated with natural convection is \(h=10\) \(\mathrm{W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The surface emissivity is \(\varepsilon=0.8\). (a) What is the rate of heat loss from the steam line? (b) If the steam is generated in a gas-fired boiler operating at an efficiency of \(\eta_{f}=0.90\) and natural gas is priced at \(C_{g}=\$ 0.02\) per \(\mathrm{MJ}\), what is the annual cost of heat loss from the line?

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