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Consider a \(300 \mathrm{kJ} / \mathrm{min}\) refrigeration system that operates on an ideal vapor-compression refrigeration cycle with refrigerant- 134 a as the working fluid. The refrigerant enters the compressor as saturated vapor at \(140 \mathrm{kPa}\) and is compressed to \(800 \mathrm{kPa}\). Show the cycle on a \(T\) -s diagram with respect to saturation lines, and determine ( \(a\) ) the quality of the refrigerant at the end of the throttling process, ( \(b\) ) the coefficient of performance, and ( \(c\) ) the power input to the compressor.

Short Answer

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b) What is the coefficient of performance (COP) of the refrigeration cycle? c) What is the power input to the compressor in kW?

Step by step solution

01

Show the cycle on a T-s diagram

To do this, first plot the saturation lines for refrigerant-134a on a T-s diagram. Then locate the four points of the cycle: 1. Saturated vapor entering the compressor at 140 kPa 2. Compressed, superheated vapor leaving the compressor at 800 kPa 3. Saturated liquid leaving the condenser 4. The refrigerant after the throttling process and before entering the evaporator. Its pressure is equal to state 1 (since it's an ideal cycle).
02

Determine the state of refrigerant-134a in each phase

Using the properties of refrigerant-134a at the given pressures, find the temperatures, specific enthalpies, and specific entropies at each state: State 1: - Pressure: \(P_1 = 140 \mathrm{kPa}\) - Since it's a saturated vapor, use tables to find \(T_1, h_1,\text{ and } s_1\). State 2: - Pressure: \(P_2 = 800 \mathrm{kPa}\) - Since it's an ideal cycle, \(s_2 = s_1\). Use tables to find \(T_2\) and \(h_2\). State 3: - Pressure: \(P_3 = 800 \mathrm{kPa}\) - Since it's a saturated liquid, use tables to find \(T_3, h_3,\text{ and } s_3\).
03

The quality of the refrigerant at the end of the throttling process (state 4)

We know that in the throttling process the enthalpy remains constant, so \(h_4 = h_3\). Since we know the pressure and enthalpy of state 4 (\(P_4 = 140 \mathrm{kPa}\) and \(h_4 = h_3\)), we can use the refrigerant property tables to find the quality of the refrigerant at state 4, \(x_4\): $$ x_4 = \frac{h_4 - h_{f,4}}{h_{g,4} - h_{f,4}} $$
04

Calculate the coefficient of performance (COP)

The COP of a refrigeration cycle is defined as the ratio of the heat removed from the substance being cooled (Q_in) to the work input to the compression cycle (W_comp): $$ \text{COP} = \frac{Q_\text{in}}{W_\text{comp}} $$ We can find \(Q_\text{in}\) by using the mass flow rate, \(m_\text{dot}\) and the difference in enthalpies between state 1 and state 4: $$ Q_\text{in} = m_\text{dot}(h_1 - h_4) $$ We can find \(W_\text{comp}\) by using the mass flow rate, \(m_\text{dot}\) and the difference in enthalpies between state 1 and state 2: $$ W_\text{comp} = m_\text{dot}(h_2 - h_1) $$ To find the mass flow rate, we can use the cooling capacity, which is equal to \(Q_\text{in}\): $$ m_\text{dot} = \frac{300 \,\mathrm{kJ/min}}{(h_1 - h_4) \cdot 60 \,\mathrm{s/min}} $$ Finally, substitute the derived expressions for \(Q_\text{in}\) and \(W_\text{comp}\) in the COP equation.
05

Calculate the power input to the compressor

Using the derived expression for \(W_\text{comp}\): $$ W_\text{comp} = m_\text{dot}(h_2 - h_1) $$ Calculate the power input to the compressor by substituting the calculated mass flow rate, \(m_\text{dot}\) and the specific enthalpies, \(h_1\) and \(h_2\). Note that the unit of the power input will be kW.

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Most popular questions from this chapter

Devise a refrigeration cycle that works on the reversed Stirling cycle. Also, determine the COP for this cycle.

A reversible absorption refrigerator consists of a reversible heat engine and a reversible refrigerator. The system removes heat from a cooled space at \(-15^{\circ} \mathrm{C}\) at a rate of \(70 \mathrm{kW}\) The refrigerator operates in an environment at \(25^{\circ} \mathrm{C}\). If the heat is supplied to the cycle by condensing saturated steam at \(150^{\circ} \mathrm{C},\) determine \((a)\) the rate at which the steam condenses, and (b) the power input to the reversible refrigerator. (c) If the COP of an actual absorption chiller at the same temperature limits has a COP of \(0.8,\) determine the second-law efficiency of this chiller.

A refrigeration system operates on the ideal vaporcompression refrigeration cycle with ammonia as the refrigerant. The evaporator and condenser pressures are \(200 \mathrm{kPa}\) and \(2000 \mathrm{kPa}\), respectively. The temperatures of the lowtemperature and high-temperature mediums are \(-9^{\circ} \mathrm{C}\) and \(27^{\circ} \mathrm{C},\) respectively. If the rate of heat rejected in the condenser is \(18.0 \mathrm{kW}\), determine ( \(a\) ) the volume flow rate of ammonia at the compressor inlet, in \(\mathrm{L} / \mathrm{s},(b)\) the power input and the \(\mathrm{COP}\) and \((c)\) the second-law efficiency of the cycle and the total exergy destruction in the cycle. The properties of ammonia at various states are given as follows: \(h_{1}=1439.3 \mathrm{kJ} / \mathrm{kg}\) \(s_{1}=5.8865 \mathrm{kJ} / \mathrm{kg} \cdot \mathrm{K}, v_{1}=0.5946 \mathrm{m}^{3} / \mathrm{kg}, h_{2}=1798.3 \mathrm{kJ} / \mathrm{kg}\) \(h_{3}=437.4 \mathrm{kJ} / \mathrm{kg}, s_{3}=1.7892 \mathrm{kJ} / \mathrm{kg} \cdot \mathrm{K}, s_{4}=1.9469 \mathrm{kJ} / \mathrm{kg} \cdot \mathrm{K}\) Note: state 1: compressor inlet, state 2: compressor exit, state 3: condenser exit, state 4 : evaporator inlet.

An aircraft on the ground is to be cooled by a gas refrigeration cycle operating with air on an open cycle. Air enters the compressor at \(30^{\circ} \mathrm{C}\) and \(100 \mathrm{kPa}\) and is compressed to \(250 \mathrm{kPa}\). Air is cooled to \(70^{\circ} \mathrm{C}\) before it enters the turbine. Assuming both the turbine and the compressor to be isentropic, determine the temperature of the air leaving the turbine and entering the cabin.

A refrigerator operates on the ideal vapor-compression refrigeration cycle and uses refrigerant-134a as the working fluid. The condenser operates at 300 psia and the evaporator at \(20^{\circ} \mathrm{F}\). If an adiabatic, reversible expansion device were available and used to expand the liquid leaving the condenser, how much would the COP improve by using this device instead of the throttle device?

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