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Refrigerant-22 absorbs heat from a cooled space at \(50^{\circ} \mathrm{F}\) as it flows through an evaporator of a refrigeration system. \(R-22\) enters the evaporator at \(10^{\circ} \mathrm{F}\) at a rate of \(0.08 \mathrm{lbm} / \mathrm{s}\) with a quality of 0.3 and leaves as a saturated vapor at the same pressure. Determine \((a)\) the rate of cooling provided, in \(\mathrm{Btu} / \mathrm{h},(b)\) the rate of exergy destruction in the evaporator, and \((c)\) the second-law efficiency of the evaporator. Take \(T_{0}\) \(=77^{\circ} \mathrm{F} .\) The properties of \(\mathrm{R}-22\) at the inlet and exit of the evaporator are: \(h_{1}=107.5 \mathrm{Btu} / \mathrm{lbm}, s_{1}=0.2851 \mathrm{Btu} / \mathrm{lbm} \cdot \mathrm{R}\) \(h_{2}=172.1 \mathrm{Btu} / \mathrm{lbm}, s_{2}=0.4225 \mathrm{Btu} / \mathrm{lbm} \cdot \mathrm{R}\)

Short Answer

Expert verified
Answer: To find these values, follow the 4-step solution provided above: 1. Calculate the heat transfer rate in the evaporator (Q) using the formula: \(Q = \dot{m} \times (h_{2} - h_{1})\) 2. Convert the heat transfer rate to Btu/h using the conversion factor 3600. 3. Calculate the rate of exergy destruction in the evaporator using the formula: \(\dot{E}_{\text{destruction}} = T_{0} \times \dot{m} \times (s_{2} - s_{1})\) 4. Calculate the second-law efficiency of the evaporator using the formula: \(\eta_{\text{II}} = 1 - \frac{\dot{E}_{\text{destruction}}}{\dot{E}_{\text{ideal}}}\) With the required calculations, you will be able to determine the rate of cooling provided (in Btu/h), the rate of exergy destruction in the evaporator, and the second-law efficiency of the evaporator.

Step by step solution

01

Calculate the heat transfer rate in the evaporator

Calculate the heat transfer rate in the evaporator, which can be determined by multiplying the mass flow rate of the refrigerant by the change in enthalpy between the inlet and outlet of the evaporator: $$Q = \dot{m} \times (h_{2} - h_{1})$$ Where: \(\dot{m}\) = mass flow rate of the refrigerant = 0.08 lbm/s \(h_{1}\) = enthalpy at the inlet = 107.5 Btu/lbm \(h_{2}\) = enthalpy at the outlet = 172.1 Btu/lbm
02

Convert the heat transfer rate to Btu/h

To find the rate of cooling provided in Btu/h, convert the Q value from Btu/s to Btu/h by multiplying it by the conversion factor 3600 (seconds in an hour): \((Q \:\text{in Btu/s}) \times 3600 = Q \:\text{in Btu/h}\)
03

Calculate the rate of exergy destruction in the evaporator

The rate of exergy destruction, can be calculated using the following formula for an open system: $$\dot{E}_{\text{destruction}} = T_{0} \times \dot{m} \times (s_{2} - s_{1})$$ Where: \(T_{0}\) = temperature of the environment = 77°F = 537.67 °R (use Rankine for consistency) \(s_{1}\) = entropy at the inlet = 0.2851 Btu/lbm·R \(s_{2}\) = entropy at the outlet = 0.4225 Btu/lbm·R
04

Calculate the second-law efficiency of the evaporator

The second-law efficiency of the evaporator is given by: $$\eta_{\text{II}} = \frac{\dot{E}_{\text{ideal}} - \dot{E}_{\text{actual}}}{\dot{E}_{\text{ideal}} - \dot{E}_{\text{destruction}}}$$ However, since the evaporator is a cooling device, the ideal rate of exergy transfer \(\dot{E}_{\text{ideal}}\) is equal to the actual rate of exergy transfer \(\dot{E}_{\text{actual}}\). Therefore, the second-law efficiency simplifies to: $$\eta_{\text{II}} = 1 - \frac{\dot{E}_{\text{destruction}}}{\dot{E}_{\text{ideal}}}$$ Now, we can calculate the second-law efficiency using the rate of exergy destruction calculated in step 3 and the actual and ideal rates of exergy transfer. After solving these steps, we will have the answers for the rate of cooling provided (in Btu/h), the rate of exergy destruction in the evaporator, and the second-law efficiency of the evaporator.

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Most popular questions from this chapter

Cold water \(\left(c_{p}=4.18 \mathrm{kJ} / \mathrm{kg} \cdot^{\circ} \mathrm{C}\right)\) leading to a shower enters a well-insulated, thin-walled, double-pipe, counterflow heat exchanger at \(15^{\circ} \mathrm{C}\) at a rate of \(0.25 \mathrm{kg} / \mathrm{s}\) and is heated to \(45^{\circ} \mathrm{C}\) by hot water \(\left(c_{p}=4.19 \mathrm{kJ} / \mathrm{kg} \cdot^{\circ} \mathrm{C}\right)\) that enters at \(100^{\circ} \mathrm{C}\) at a rate of \(3 \mathrm{kg} / \mathrm{s}\). Determine \((a)\) the rate of heat transfer and \((b)\) the rate of exergy destruction in the heat exchanger. Take \(T_{0}=25^{\circ} \mathrm{C}\)

A piston-cylinder device initially contains \(1.4 \mathrm{kg}\) of refrigerant-134a at \(100 \mathrm{kPa}\) and \(20^{\circ} \mathrm{C}\). Heat is now transferred to the refrigerant from a source at \(150^{\circ} \mathrm{C}\), and the piston which is resting on a set of stops, starts moving when the pressure inside reaches \(120 \mathrm{kPa}\). Heat transfer continues until the temperature reaches \(80^{\circ} \mathrm{C}\). Assuming the surroundings to be at \(25^{\circ} \mathrm{C}\) and \(100 \mathrm{kPa}\), determine \((a)\) the work done, (b) the heat transfer, \((c)\) the exergy destroyed, and \((d)\) the second- law efficiency of this process. Answers: (a) \(0.497 \mathrm{kJ},\) (b) \(67.9 \mathrm{kJ}\).

Chickens with an average mass of \(1.6 \mathrm{kg}\) and average specific heat of \(3.54 \mathrm{kJ} / \mathrm{kg} \cdot^{\circ} \mathrm{C}\) are to be cooled by chilled water that enters a continuous-flow-type immersion chiller at \(0.5^{\circ} \mathrm{C}\) and leaves at \(2.5^{\circ} \mathrm{C}\). Chickens are dropped into the chiller at a uniform temperature of \(15^{\circ} \mathrm{C}\) at a rate of 700 chickens per hour and are cooled to an average temperature of \(3^{\circ} \mathrm{C}\) before they are taken out. The chiller gains heat from the surroundings at a rate of \(400 \mathrm{kJ} / \mathrm{h}\). Determine \((a)\) the rate of heat removal from the chicken, in \(\mathrm{kW},\) and \((b)\) the rate of exergy destruction during this chilling process. Take \(T_{0}=25^{\circ} \mathrm{C}\)

\(8-74 \quad\) A \(0.6-m^{3}\) rigid tank is filled with saturated liquid water at \(170^{\circ} \mathrm{C}\). A valve at the bottom of the tank is now opened, and one-half of the total mass is withdrawn from the tank in liquid form. Heat is transferred to water from a source of \(210^{\circ} \mathrm{C}\) so that the temperature in the tank remains constant. Determine \((a)\) the amount of heat transfer and \((b)\) the reversible work and exergy destruction for this process. Assume the surroundings to be at \(25^{\circ} \mathrm{C}\) and \(100 \mathrm{kPa}\).

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