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An air conditioner operating between indoor and outdoor temperatures of 23 and \(43^{\circ} \mathrm{C}\), respectively, removes \(5 \mathrm{~kW}\) from a building. The air conditioner can be modeled as a reversed Carnot heat engine with refrigerant as the working fluid. The efficiency of the motor for the compressor and fan is \(80 \%\), and \(0.2 \mathrm{~kW}\) is required to operate the fan. (a) Assuming negligible thermal resistances (Problem 11.73) between the refrigerant in the condenser and the outside air and between the refrigerant in the evaporator and the inside air, calculate the power required by the motor. (b) If the thermal resistances between the refrigerant and the air in the evaporator and condenser sections are the same, \(3 \times 10^{-3} \mathrm{~K} / \mathrm{W}\), determine the temperature required by the refrigerant in each section. Calculate the power required by the motor.

Short Answer

Expert verified
(a) For negligible thermal resistance, the power required by the motor is \(0.6216\,kW\). (b) For the given thermal resistance, the temperatures required by the refrigerant are \(296.165\,K\) in the evaporator and \(316.135\,K\) in the condenser, and the power required by the motor is \(0.6220\,kW\).

Step by step solution

01

Calculate the ideal coefficient of performance for the air conditioner

The coefficient of performance (COP) indicates how efficient an air conditioner is in transferring heat. Using the COP formula for the reversible Carnot cycle gives: \[COP_{ideal} = \frac{Q_L}{W_{in}} = \frac{T_L}{T_H - T_L}\] Where: \(Q_L\) = Heat extracted from the building \(W_{in}\) = Work input to the air conditioner \(T_L\) = Indoor temperature in kelvin \(T_H\) = Outdoor temperature in kelvin First, let's convert the given temperature in Celsius to Kelvin: \(T_L = 23 + 273.15 = 296.15\,K\) \(T_H = 43 + 273.15 = 316.15\,K\) Now, we can calculate the ideal coefficient of performance: \[COP_{ideal} = \frac{296.15}{316.15 - 296.15} = 14.8075\]
02

Calculate the power input required in the ideal case

To keep the calculation simple, we'll assume a heat transfer rate of \(Q_L = 5\,kW\). Using the coefficient of performance calculated in Step 1, we can compute the power input for the air conditioner: \[W_{in} = \frac{Q_L}{COP_{ideal}} = \frac{5\,kW}{14.8075} = 0.3373\,kW\]
03

Calculate the power input for motor efficiency

Since the motor efficiency is given as 80%, we need to adjust the calculated power input for this efficiency using the following equation: \[W_{motor} = \frac{W_{in}}{motor\:efficiency} = \frac{0.3373\,kW}{0.8} = 0.4216\,kW\] In addition, it's given that the fan requires a power input of 0.2 kW.
04

Calculate the total power input required

Now, adding the power input needed for the fan, we get the total power input required for the motor: \[W_{total} = W_{motor} + W_{fan} = 0.4216 + 0.2 = 0.6216\,kW\] With negligible thermal resistance, the motor must deliver 0.6216 kW of power to operate the air conditioner. #Case 2: Thermal resistance \(R = 3 \times 10^{-3}\,K/W\)
05

Calculate the required temperatures for the refrigerant

With the thermal resistance given, we must find how much temperature difference is required in both evaporator and condenser sections. The heat transfer rates in the evaporator and condenser are equal, so the temperature difference must be the same in both sections: \[T_{refrigerant, evaporator} - T_L = T_H - T_{refrigerant, condenser}\] where \(T_{refrigerant, evaporator}\) = Temperature of the refrigerant in the evaporator \(T_{refrigerant, condenser}\) = Temperature of the refrigerant in the condenser Using the given thermal resistance value and the heat transfer rate, we can compute the required temperature differences: \[\Delta T = Q_L \times R = 5\,kW \times 3 \times 10^{-3}\,K/W = 0.015\,K\]
06

Find new values of \(T_L \) and \(T_H\)

By adding the computed temperature difference to the given values of \(T_L\) and \(T_H\), we can find the values of \(T_{refrigerant, evaporator}\) and \(T_{refrigerant, condenser}\): \[T_{refrigerant, evaporator} = T_L + \Delta T = 296.15 + 0.015 = 296.165\,K\] \[T_{refrigerant, condenser} = T_H - \Delta T = 316.15 - 0.015 = 316.135\,K\]
07

Calculate the new ideal coefficient of performance for the air conditioner

Using the new values of \(T_L\) and \(T_H\) in the COP formula: \[COP_{new, ideal} = \frac{296.165}{316.135 - 296.165} = 14.8146\]
08

Calculate the new power input required

With the new ideal COP, we can compute the updated power input for the air conditioner as follows: \[W_{in} = \frac{Q_L}{COP_{new, ideal}} = \frac{5\,kW}{14.8146} = 0.3376\,kW\]
09

Calculate the updated power input for motor efficiency

Adjusting the new power input for the given motor efficiency: \[W_{motor} = \frac{W_{in}}{motor\:efficiency} = \frac{0.3376\,kW}{0.8} = 0.4220\,kW\]
10

Calculate the new total power input required

Finally, adding the power input needed to operate the fan, we get: \[W_{total} = W_{motor} + W_{fan} = 0.4220 + 0.2 = 0.6220\,kW\] With the given thermal resistance, the motor must deliver 0.6220 kW of power to operate the air conditioner. #Result# (a) For negligible thermal resistance, the power required by the motor is 0.6216 kW. (b) For the given thermal resistance, the temperatures required by the refrigerant are 296.165 K in the evaporator and 316.135 K in the condenser, and the power required by the motor is 0.6220 kW.

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Key Concepts

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

Coefficient of Performance
Understanding the Coefficient of Performance (COP) is crucial when analyzing the efficiency of heat engines and refrigerators. In essence, COP is a measure of the effectiveness of a heat pump or air-conditioning system in transferring heat relative to the work input. For an air conditioner, higher COP values indicate better efficiency, meaning the system requires less energy to transfer a certain amount of heat.

The formula for COP is typically written as: \[COP = \frac{Q_L}{W_{in}}\], where \(Q_L\) represents the heat extracted by the air conditioner (the cooling load) and \(W_{in}\) denotes the work or energy input needed to transfer that heat. When applying this to a theoretical Carnot cycle, which is a perfect reversible cycle, COP is calculated using the temperatures of the hot (\(T_H\)) and cold (\(T_L\)) reservoirs: \[COP_{Carnot} = \frac{T_L}{T_H - T_L}\].

The 'ideal' COP calculated during the textbook exercise represents the maximum theoretical efficiency of the air conditioner. Under real-world conditions, the actual COP is lower due to various inefficiencies and losses. The exercise demonstrates that even a minute change in operating temperatures, such as those introduced by thermal resistance, can slightly affect the COP and, consequently, the power requirements for an air conditioner.
Thermal Resistance
The concept of Thermal Resistance (R) is analogous to electrical resistance, but it applies to heat transfer instead of electric currents. It quantifies the difficulty with which heat flows through a material or across boundaries in a system. The rate of heat transfer (\(Q\)) through a material with a thermal resistance (\(R\)) is inversely proportional to that resistance when there's a temperature difference (\(\Delta T\)) driving the flow, as stated by Fourier's law.

In the given exercise, thermal resistance determines the additional temperature difference needed for the same amount of heat to be transferred, when compared to the case with no resistance. A thermal resistance of \(3 \times 10^{-3}\) K/W means for each watt of heat transferred, a temperature difference of \(0.003\) K is required. This can significantly affect the efficiency and power requirements of HVAC systems.

The exercise improvement advice suggests understanding how equal thermal resistances in both the evaporator and condenser can lead to additional energy consumption to maintain the same heat transfer rate. This illustrates the importance of designing systems to minimize thermal resistance for energy efficiency, maintaining the desired temperature difference and reducing the overall power consumption.
Heat Transfer
The phenomenon of Heat Transfer is fundamental to understanding how energy in the form of heat moves from one place to another. In HVAC systems like air conditioners, the goal is to transfer heat from indoors to the outside environment efficiently. Heat transfers through three primary mechanisms: conduction, convection, and radiation.

In the context of the reversed Carnot engine, which models the air conditioner in this exercise, convection plays a major role as it involves the movement of the refrigerant fluid, which absorbs heat from the indoor space and releases it outdoors. The rate of heat transfer, often denoted by \(Q\), directly affects thermal machines' performance. For instance, an air conditioner that transfers \(5\text{kW}\) of heat from the inside of a building to the outside is moving a sizeable amount of energy, leading to a detectable cooling effect.

Enhancing students' understanding of heat transfer concepts is essential, including how thermal resistance and temperature gradients affect the efficiency of such processes. The exercise effectively ties together these concepts, showing that the ability of the air conditioner to maintain comfortable indoor temperatures relies on how well it can transfer the unwanted heat to the outdoor environment.

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Most popular questions from this chapter

In open heart surgery under hypothermic conditions, the patient's blood is cooled before the surgery and rewarmed afterward. It is proposed that a concentric tube, counterflow heat exchanger of length \(0.5 \mathrm{~m}\) be used for this purpose, with the thin-walled inner tube having a diameter of \(55 \mathrm{~mm}\). The specific heat of the blood is \(3500 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\). (a) If water at \(T_{h j}=60^{\circ} \mathrm{C}\) and \(\dot{m}_{h}=0.10 \mathrm{~kg} / \mathrm{s}\) is used to heat blood entering the exchanger at \(T_{c A}=18^{\circ} \mathrm{C}\) and \(\dot{m}_{c}=0.05 \mathrm{~kg} / \mathrm{s}\), what is the temperature of the blood leaving the exchanger? The overall heat transfer coefficient is \(500 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). (b) The surgeon may wish to control the heat rate \(q\) and the outlet temperature \(T_{c, 0}\) of the blood by altering the flow rate and/or inlet temperature of the water during the rewarming process. To assist in the development of an appropriate controller for the prescribed values of \(\hat{m}_{c}\) and \(T_{c \jmath}\), compute and plot \(q\) and \(T_{c, \rho}\) as a function of \(\dot{m}_{h}\) for \(0.05 \leq \dot{m}_{\mathrm{h}} \leq 0.20 \mathrm{~kg} / \mathrm{s}\) and values of \(T_{h, l}=50,60\), and \(70^{\circ} \mathrm{C}\). Since the dominant influence on the overall heat transfer coefficient is associated with the blood flow conditions, the value of \(U\) may be assumed to remain at \(500 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Should certain operating conditions be excluded?

Consider a Rankine cycle with saturated steam leaving the boiler at a pressure of \(2 \mathrm{MPa}\) and a condenser pressure of \(10 \mathrm{kPa}\). (a) Calculate the thermal efficiency of the ideal Rankine cycle for these operating conditions. (b) If the net reversible work for the cycle is \(0.5 \mathrm{MW}\), calculate the required flow rate of cooling water supplied to the condenser at \(15^{\circ} \mathrm{C}\) with an allowable temperature rise of \(10^{\circ} \mathrm{C}\). (c) Design a shell-and-tube heat exchanger (one-shell, multiple-tube passes) that will meet the heat rate and temperature conditions required of the condenser. Your design should specify the number of tubes and their diameter and length.

It is proposed that the exhaust gas from a natural gas-powered electric generation plant be used to generate steam in a shell-and-tube heat exchanger with one shell and one tube pass. The steel tubes have a thermal conductivity of \(40 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), an inner diameter of \(50 \mathrm{~mm}\), and a wall thickness of \(4 \mathrm{~mm}\). The exhaust gas, whose flow rate is \(2 \mathrm{~kg} / \mathrm{s}\), enters the heat exchanger at \(400^{\circ} \mathrm{C}\) and must leave at \(215^{\circ} \mathrm{C}\). To limit the pressure drop within the tubes, the tube gas velocity should not exceed \(25 \mathrm{~m} / \mathrm{s}\). If saturated water at \(11.7\) bar is supplied to the shell side of the exchanger, determine the required number of tubes

A cross-flow heat exchanger used in a cardiopulmonary bypass procedure cools blood flowing at \(5 \mathrm{~L} / \mathrm{min}\) from a body temperature of \(37^{\circ} \mathrm{C}\) to \(25^{\circ} \mathrm{C}\) in order to induce body hypothermia, which reduces metabolic and oxygen requirements. The coolant is ice water at \(0^{\circ} \mathrm{C}\), and its flow rate is adjusted to provide an outlet temperature of \(15^{\circ} \mathrm{C}\). The heat exchanger operates with both fluids unmixed, and the overall heat transfer coefficient is \(750 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The density and specific heat of the blood are \(1050 \mathrm{~kg} / \mathrm{m}^{3}\) and \(3740 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\), respectively. a) Determine the heat transfer rate for the exchanger. b) Calculate the water flow rate. c) What is the surface area of the heat exchanger? d) Calculate and plot the blood and water outlet temperatures as a function of the water flow rate for the range 2 to \(4 \mathrm{~L} / \mathrm{min}\), assuming all other parameters remain unchanged. Comment on how the changes in the outlet temperatures are affected by changes in the water flow rate. Explain this behavior and why it is an advantage for this application.

A counterflow, concentric tube heat exchanger is designed to heat water from 20 to \(80^{\circ} \mathrm{C}\) using hot oil, which is supplied to the annulus at \(160^{\circ} \mathrm{C}\) and discharged at \(140^{\circ} \mathrm{C}\). The thin-walled inner tube has a diameter of \(D_{i}=20 \mathrm{~mm}\), and the overall heat transfer coefficient is \(500 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The design condition calls for a total heat transfer rate of \(3000 \mathrm{~W}\). (a) What is the length of the heat exchanger? (b) After 3 years of operation, performance is degraded by fouling on the water side of the exchanger, and the water outlet temperature is only \(65^{\circ} \mathrm{C}\) for the same fluid flow rates and inlet temperatures. What are the corresponding values of the heat transfer rate, the outlet temperature of the oil, the overall heat transfer coefficient, and the water- side fouling factor, \(R_{f,}^{n}\) ?

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