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Can a vapor-compression refrigeration system with a single compressor handle several evaporators operating at different pressures? How?

Short Answer

Expert verified
Answer: Yes, a single compressor vapor-compression refrigeration system can handle multiple evaporators operating at different pressures by implementing a multi-evaporator system with individual expansion valves for each evaporator to regulate refrigerant flow and pressure.

Step by step solution

01

Definition of a Vapor-Compression Refrigeration System

A vapor-compression refrigeration system typically consists of a compressor, condenser, evaporator, and expansion valve. The compressor pumps the refrigerant throughout the system, the condenser releases heat to the environment, the evaporator absorbs heat from the refrigeration space, and the expansion valve regulates the refrigerant flow from the high-pressure side to the low-pressure side.
02

Understanding the Components

A single compressor is a vital component in the vapor-compression refrigeration system, maintaining the pressure difference and promoting the refrigerant flow throughout the system. However, for the system to handle several evaporators operating at different pressures, it is essential to modify the system slightly.
03

Multi-Evaporator System

A solution to accommodate several evaporators within one system is to use a multi-evaporator system with individual expansion valves for each evaporator. The expansion valves regulate the refrigerant flow from the common high-pressure side (condenser) to each evaporator, allowing them to operate at different pressures.
04

How It Works

In a multi-evaporator system, each evaporator has its expansion valve. After the condenser, the refrigerant liquid is split into multiple paths, with each path leading to an expansion valve and then to a different evaporator. The expansion valves help maintain the desired pressure level and control the refrigerant flow rate for each evaporator. After the refrigerant leaves the evaporators, the multiple paths rejoin, and the refrigerant vapor is directed to the single compressor, which then compresses it and sends it back to the condenser.
05

Conclusion

Yes, a vapor-compression refrigeration system with a single compressor can handle several evaporators operating at different pressures. It can be achieved by implementing a multi-evaporator system with individual expansion valves for each evaporator, helping regulate refrigerant flow and pressure.

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Most popular questions from this chapter

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.

Consider a two-stage cascade refrigeration system operating between the pressure limits of \(1.2 \mathrm{MPa}\) and \(200 \mathrm{kPa}\) with refrigerant-134a as the working fluid. The refrigerant leaves the condenser as a saturated liquid and is throttled to a flash chamber operating at 0.45 MPa. Part of the refrigerant evaporates during this flashing process, and this vapor is mixed with the refrigerant leaving the low-pressure compressor. The mixture is then compressed to the condenser pressure by the high-pressure compressor. The liquid in the flash chamber is throttled to the evaporator pressure and cools the refrigerated space as it vaporizes in the evaporator. The mass flow rate of the refrigerant through the lowpressure compressor is \(0.15 \mathrm{kg} / \mathrm{s}\). Assuming the refrigerant leaves the evaporator as a saturated vapor and the isentropic efficiency is 80 percent for both compressors, determine \((a)\) the mass flow rate of the refrigerant through the high-pressure compressor, \((b)\) the rate of heat removal from the refrigerated space, and \((c)\) the COP of this refrigerator. Also, determine \((d)\) the rate of heat removal and the COP if this refrigerator operated on a single-stage cycle between the same pressure limits with the same compressor efficiency and the same flow rate as in part ( \(a\) ).

Air enters the compressor of an ideal gas refrigeration cycle at \(7^{\circ} \mathrm{C}\) and \(35 \mathrm{kPa}\) and the turbine at \(37^{\circ} \mathrm{C}\) and \(160 \mathrm{kPa}\). The mass flow rate of air through the cycle is \(0.2 \mathrm{kg} / \mathrm{s}\). Assuming variable specific heats for air, determine ( \(a\) ) the rate of refrigeration, \((b)\) the net power input, and \((c)\) the coefficient of performance.

It is proposed to run a thermoelectric generator in conjunction with a solar pond that can supply heat at a rate of \(7 \times 10^{6} \mathrm{kJ} / \mathrm{h}\) at \(90^{\circ} \mathrm{C}\). The waste heat is to be rejected to the environment at \(22^{\circ} \mathrm{C}\). What is the maximum power this thermoelectric generator can produce?

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.

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