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An ideal vapor-compression heat pump cycle with Refrigerant \(134 \mathrm{a}\) as the working fluid provides heating at a rate of \(15 \mathrm{~kW}\) to maintain a building at \(20^{\circ} \mathrm{C}\) when the outside temperature is \(5^{\circ} \mathrm{C}\). Saturated vapor at \(2.4\) bar leaves the evaporator, and saturated liquid at 8 bar leaves the condenser. Calculate (a) the power input to the compressor, in \(\mathrm{kW}\). (b) the coefficient of performance. (c) the coefficient of performance of a Carnot heat pump cycle operating between thermal reservoirs at 20 and \(5^{\circ} \mathrm{C}\).

Short Answer

Expert verified
Power input to the compressor is 2.01 kW, COP is 7.46, and Carnot COP is 19.54.

Step by step solution

01

- Determine properties from tables

Identify the relevant thermodynamic states for the refrigerant from the provided conditions: saturated vapor at 2.4 bar and saturated liquid at 8 bar. Use refrigerant tables to find the enthalpies at these states. Let's denote the state before the compressor as state 1 and after the compressor as state 2.
02

- Find enthalpies

From refrigerant tables: For saturated vapor at 2.4 bar (state 1): \(h_1 = 396 \text{ kJ/kg} \). For saturated liquid at 8 bar: \(h_3 = 248 \text{ kJ/kg} \).
03

- Use isentropic process

Assuming an isentropic process for the compressor, use the entropy values: For saturated vapor at 2.4 bar: \(s_1 = 1.250 \text{ kJ/kg·K} \). Then find the enthalpy after compression (state 2) using the isentropic relation: \(s_1 = s_2\), find out from the tables or diagrams: \(h_2 = 419 \text{ kJ/kg} \).
04

- Calculate the mass flow rate

Using the given heating rate (\(\text{Q} = 15 \text{ kW} \)) and the enthalpy change in the condenser: \( Q = \text{m} \times (h_2 - h_3) \). Solve for m: \( \text{m} = \frac{Q}{(h_2 - h_3)} = \frac{15}{(419 - 248)} = 0.0877 \text{ kg/s} \).
05

- Calculate power input to the compressor

Use the mass flow rate to find the power input to the compressor: \( \text{Power input} = \text{m} \times (h_2 - h_1) = 0.0877 \times (419 - 396) = 2.01 \text{ kW} \).
06

- Calculate the Coefficient of Performance (COP)

COP for the heat pump cycle is given by: \( \text{COP} = \frac{Q}{\text{Power input}} = \frac{15}{2.01} = 7.46 \).
07

- Calculate the COP of a Carnot heat pump cycle

For the Carnot heat pump, use temperatures in Kelvin: \( \text{T}_{\text{hot}} = 20 + 273.15 = 293.15 \text{ K} \) and \( \text{T}_{\text{cold}} = 5 + 273.15 = 278.15 \text{ K} \). \( \text{COP}_{\text{Carnot}} = \frac{T_{\text{hot}}}{T_{\text{hot}} - T_{\text{cold}}} = \frac{293.15}{293.15 - 278.15} = 19.54 \).

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Key Concepts

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

Isentropic Process
In the context of a vapor-compression heat pump cycle, an isentropic process is one where the entropy remains constant. Entropy is a measure of disorder or randomness in a system. For the compressor in our heat pump cycle, we assume it undergoes an isentropic process, meaning no entropy is generated within the compressor.

This isentropic assumption simplifies calculations and represents an ideal situation where the process is both adiabatic (no heat transfer) and reversible.

Key points in isentropic process:
  • Entropy before and after the compressor remains the same: \[ s_1 = s_2 \]
  • We utilize refrigerant tables or diagrams to obtain properties such as enthalpy and entropy for the refrigerant.
  • This assumption allows us to use known values to find unknowns, making calculation straightforward and eliminating the need for more complex, real-world considerations like friction and heat losses.
The process, therefore, is critical in determining the enthalpy after compression, which is necessary for calculating things like power input to the compressor and ultimately the system's efficiency.
Enthalpy Calculation
Enthalpy is a measure of the total energy of a system, including both its internal energy and the product of its pressure and volume. In our vapor-compression heat pump cycle, calculating enthalpy at various points in the cycle is crucial for analyzing the system.

Steps for calculating enthalpy:
  • Use refrigerant tables to find the enthalpy values corresponding to specific states of the refrigerant.
  • For the given problem, state 1 involves saturated vapor at 2.4 bar with an enthalpy: \[ h_1 = 396 \text{ kJ/kg} \]
  • State 3 concerns saturated liquid at 8 bar with an enthalpy: \[ h_3 = 248 \text{ kJ/kg} \]
  • Using the isentropic assumption, we can find the enthalpy after compression (state 2) since \[ s_1 = s_2 \] leading to: \[ h_2 = 419 \text{ kJ/kg} \]
  • These enthalpy values are then used to determine the mass flow rate and various power requirements.
Calculation steps can be summarized as:
  • Obtain enthalpy values at different states from refrigerant tables.
  • Use these values in energy balance equations to calculate quantities like mass flow rate and power input.
Enthalpy calculations link the thermodynamic properties of the refrigerant with the performance parameters of the heat pump system.
Coefficient of Performance
The Coefficient of Performance (COP) for a heat pump is a measure of its efficiency. It indicates how effectively the heat pump uses work input to transfer heat. A higher COP means higher efficiency.

Calculating COP:
  • The general formula for COP in a heating mode: \[ \text{COP} = \frac{Q}{\text{Power Input}} \]
  • In our problem, Q is the heating rate provided to the building, which is 15 kW, and the power input to the compressor is found to be 2.01 kW.
  • Using these values, the COP is:\[ \text{COP} = \frac{15}{2.01} = 7.46 \]
  • This means the heat pump delivers 7.46 units of heat for every unit of work.
Additionally, comparing this to the ideal Carnot heat pump cycle, which operates between specific temperatures (20°C and 5°C) and has a very high COP:
  • Using the Carnot COP formula:\[ \text{COP}_{\text{Carnot}} = \frac{T_{\text{hot}}}{T_{\text{hot}} - T_{\text{cold}}} \]
  • Convert temperatures to Kelvin (Thot = 293.15 K and Tcold = 278.15 K):
  • The Carnot COP is:\[ \text{COP}_{\text{Carnot}} = \frac{293.15}{293.15 - 278.15} = 19.54 \]
Real systems, like our vapor-compression heat pump, have lower COPs than the ideal Carnot cycle due to practical inefficiencies. Understanding COP helps in evaluating how well a heat pump performs and where improvements might be made.

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Most popular questions from this chapter

A vapor-compression refrigeration system circulates Refrigerant \(134 \mathrm{a}\) at a rate of \(6 \mathrm{~kg} / \mathrm{min}\). The refrigerant enters the compressor at \(-10^{\circ} \mathrm{C}, 1.4\) bar, and exits at 7 bar. The isentropic compressor efficiency is \(67 \%\). There are no appreciable pressure drops as the refrigerant flows through the condenser and evaporator. The refrigerant leaves the condenser at 7 bar, \(24^{\circ} \mathrm{C}\). Ignoring heat transfer between the compressor and its surroundings, determine (a) the coefficient of performance. (b) the refrigerating capacity, in tons. (c) the rates of exergy destruction in the compressor and expansion valve, each in \(\mathrm{kW}\). (d) the changes in specific flow exergy of the refrigerant passing through the evaporator and condenser, respectively, each in \(\mathrm{kJ} / \mathrm{kg}\). Let \(T_{0}=21^{\circ} \mathrm{C}, p_{0}=1\) bar.

\(10.34\) Air at 2 bar, \(380 \mathrm{~K}\) is extracted from a main jet engine compressor for cabin cooling. The extracted air enters a heat exchanger where it is cooled at constant pressure to \(320 \mathrm{~K}\) through heat transfer with the ambient. It then expands adiabatically to \(0.95\) bar through a turbine and is discharged into the cabin. The turbine has an isentropic efficiency of \(75 \% .\) If the mass flow rate of the air is \(1.0 \mathrm{~kg} / \mathrm{s}\), determine (a) the power developed by the turbine, in \(\mathrm{kW}\). (b) the rate of heat transfer from the air to the ambient, in \(\mathrm{kW}\).

An ideal vapor-compression refrigeration cycle, with ammonia as the working fluid, has an evaporator temperature of \(-20^{\circ} \mathrm{C}\) and a condenser pressure of 12 bar. Saturated vapor enters the compressor, and saturated liquid exits the condenser. The mass flow rate of the refrigerant is \(3 \mathrm{~kg} / \mathrm{min}\). Determine (a) the coefficient of performance. (b) the refrigerating capacity, in tons.

A vapor-compression refrigeration system with a capacity of 10 tons has superheated Refrigerant 134 a vapor entering the compressor at \(15^{\circ} \mathrm{C}, 4\) bar, and exiting at 12 bar. The compression process can be modeled by \(p v^{1.01}=\) constant. At the condenser exit, the pressure is \(11.6\) bar, and the temperature is \(44^{\circ} \mathrm{C}\). The condenser is water-cooled, with water entering at \(20^{\circ} \mathrm{C}\) and leaving at \(30^{\circ} \mathrm{C}\) with a negligible change in pressure. Heat transfer from the outside of the condenser can be neglected. Determine (a) the mass flow rate of the refrigerant, in \(\mathrm{kg} / \mathrm{s}\). (b) the power input and the heat transfer rate for the compressor, each in \(\mathrm{kW}\). (c) the coefficient of performance. (d) the mass flow rate of the cooling water, in \(\mathrm{kg} / \mathrm{s}\). (e) the rates of exergy destruction in the condenser and expansion valve, each expressed as a percentage of the power input. Let \(T_{0}=20^{\circ} \mathrm{C}\).

Air enters the compressor of an ideal Brayton refrigeration cycle at \(100 \mathrm{kPa}, 270 \mathrm{~K}\). The compressor pressure ratio is 3 , and the temperature at the turbine inlet is \(310 \mathrm{~K}\). Determine (a) the net work input, per unit mass of air flow, in \(\mathrm{kJ} / \mathrm{kg}\). (b) the refrigeration capacity, per unit mass of air flow, in \(\mathrm{kJ} / \mathrm{kg}\). (c) the coefficient of performance. (d) the coefficient of performance of a Carnot refrigeration cycle operating between thermal reservoirs at \(T_{C}=270 \mathrm{~K}\) and \(T_{\mathrm{H}}=310 \mathrm{~K}\), respectively.

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