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An absorption refrigeration system that receives heat from a source at \(95^{\circ} \mathrm{C}\) and maintains the refrigerated space at \(0^{\circ} \mathrm{C}\) is claimed to have a COP of \(3.1 .\) If the environmental temperature is \(19^{\circ} \mathrm{C}\), can this claim be valid? Justify your answer.

Short Answer

Expert verified
Answer: Yes, the claim is valid, as the calculated Carnot COP (3.677) is higher than the given COP (3.1), indicating that the system operates within the maximum theoretical efficiency.

Step by step solution

01

Convert temperatures to Kelvin

Since all given temperatures are in degree Celsius, we need to convert them to Kelvin using the formula \(K = ^\circ C + 273.15\). Therefore, Heat source temperature (T₁) = \(95^\circ C + 273.15 = 368.15\,\text{K}\) Refrigerated space temperature (T₃) = \(0^\circ C + 273.15 = 273.15\,\text{K}\) Environmental temperature (T₂) = \(19^\circ C + 273.15 = 292.3\,\text{K}\)
02

Calculate Carnot COP

The COP of an ideal refrigeration system is governed by the highest theoretical efficiency possible, also known as Carnot COP. Using the refrigeration Carnot COP formula, we can calculate it as: Carnot COP = \(\frac{T_3}{T_1 - T_3}\) Plug in our values: Carnot COP = \(\frac{273.15}{368.15 - 273.15} \approx 3.677\)
03

Compare given COP with Carnot COP

Since the given COP is \(3.1\) and the calculated Carnot COP is approximately \(3.677\), the given claim of a COP of \(3.1\) is less than the maximum theoretical efficiency possible (Carnot COP), and therefore, the claim is valid.

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Most popular questions from this chapter

A room is kept at \(-5^{\circ} \mathrm{C}\) by a vapor-compression refrigeration cycle with \(\mathrm{R}-134 \mathrm{a}\) as the refrigerant. Heat is rejected to cooling water that enters the condenser at \(20^{\circ} \mathrm{C}\) at a rate of \(0.13 \mathrm{kg} / \mathrm{s}\) and leaves at \(28^{\circ} \mathrm{C}\). The refrigerant enters the condenser at \(1.2 \mathrm{MPa}\) and \(50^{\circ} \mathrm{C}\) and leave as a saturated liquid. If the compressor consumes \(1.9 \mathrm{kW}\) of power, determine (a) the refrigeration load, in \(\mathrm{Btu} / \mathrm{h}\) and the \(\mathrm{COP}\), (b) the second-law efficiency of the refrigerator and the total exergy destruction in the cycle, and \((c)\) the exergy destruction in the condenser. Take \(T_{0}=20^{\circ} \mathrm{C}\) and \(c_{p \text { ,water }}=4.18 \mathrm{kJ} / \mathrm{kg} \cdot^{\circ} \mathrm{C} .\)

An ice-making machine operates on the ideal vapor-compression cycle, using refrigerant-134a. The refrigerant enters the compressor as saturated vapor at 20 psia and leaves the condenser as saturated liquid at 80 psia. Water enters the ice machine at \(55^{\circ} \mathrm{F}\) and leaves as ice at \(25^{\circ} \mathrm{F}\). For an ice production rate of \(15 \mathrm{lbm} / \mathrm{h}\), determine the power input to the ice machine \((169 \mathrm{Btu}\) of heat needs to be removed from each \(1 \mathrm{bm}\) of water at \(55^{\circ} \mathrm{F}\) to turn it into ice at \(25^{\circ} \mathrm{F}\) ).

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

Consider a steady-flow Carnot refrigeration cycle that uses refrigerant-134a as the working fluid. The maximum and minimum temperatures in the cycle are 30 and \(-20^{\circ} \mathrm{C}\) respectively. The quality of the refrigerant is 0.15 at the beginning of the heat absorption process and 0.80 at the end. Show the cycle on a \(T\) -s diagram relative to saturation lines, and determine (a) the coefficient of performance, ( \(b\) ) the condenser and evaporator pressures, and ( \(c\) ) the net work input.

How does the COP of a cascade refrigeration system compare to the COP of a simple vapor-compression cycle operating between the same pressure limits?

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