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Modern Engineering Thermodynamics

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358 CHAPTER 10: Availability Analysis<br />

70. The turbine of a large power plant receives 1.00 × 10 8 Btu/h of<br />

heat from the boiler at 900.°F and rejects 5.50 × 10 6 Btu/h of<br />

heat to the condenser at 60.0°F while producing 22.0 × 10 3 kW<br />

of electrical power. The local environment (ground state) is at<br />

14.7 psia and 50.0°F. Determine<br />

a. The first law thermal efficiency.<br />

b. The rate at which available energy enters the boiler.<br />

c. The rate at which available energy enters the condenser.<br />

d. The second law availability efficiency of the power plant.<br />

71. The Heat-Master is a new heat pump design that has a Carnot<br />

COP (coefficient of performance) of 15.5. However, its actual<br />

coefficient of performance is only 6.90. Determine the second<br />

law availability efficiency of this heat pump.<br />

72.* A heat pump is designed to provide 9.00 kW of heat to a<br />

small house at 20.0°C when the outside temperature is 5.00°C.<br />

The electric motor driving the heat pump draws 1.20 kW.<br />

Determine:<br />

a. The first law thermal efficiency (i.e., COP) of the heat pump.<br />

b. The second law availability efficiency of the heat pump.<br />

73. The Cool-Master is a new window air conditioner design that<br />

has a Carnot coefficient of performance (COP) of 18.9.<br />

However, its actual coefficient of performance is only 3.30.<br />

Determine the second law availability efficiency of this air<br />

conditioner.<br />

74. A common window air conditioner has an actual COP of<br />

7.88. If the inside temperature is T 0 = T L = 75.0°F andthe<br />

outside temperature is 95.0°F, then determine the second<br />

law availability efficiency of this air conditioner.<br />

75. Liquid water is to be heated in a nonmixing heat exchanger<br />

with waste steam. The liquid water (an incompressible liquid)<br />

flows through the heat exchanger at 15.0 lbm/s with an inlet<br />

temperature of 50.0°F and an exit temperature of 75.0°F. The<br />

steam flows through the heat exchanger at 3.00 lbm/s with an<br />

inlet state of 600.°F and 60.0 psia and an exit state of 400.°F<br />

and 40.0 psia. Determine the second law availability efficiency<br />

of this heat exchanger. Neglect all kinetic and potential energy<br />

effects, and use saturated liquid water at 50.0°F as the local<br />

environment (ground state).<br />

76. The inlet air to a gas turbine engine is preheated with the<br />

engine’s exhaust gases. The preheater is insulated so that all<br />

heat transfer is internal. The engine’s exhaust gas enters the<br />

preheater at 800.°F and 1.30 atm pressure and exits at 500.°F<br />

and 1.00 atm. The inlet air enters the preheater at 70.0°F and<br />

1.40 atm and exits at 1.30 atm. The mass flow rates of the<br />

inlet air and the exiting exhaust are approximately the same at<br />

2.10 lbm/s. Both gases can be treated as constant specific heat<br />

ideal gases. The specific heat and gas constant of the exhaust<br />

gas are (c p ) exh. = 0.238 Btu/(lbm·R) and R exh. = 0.0640 Btu/<br />

(lbm·R). Neglecting all kinetic and potential energies, and<br />

taking the local environment (ground state) as p 0 = 1.00 atm,<br />

and T 0 = 70.0°F, determine:<br />

a. The exit temperature of the inlet air.<br />

b. The second law availability efficiency of the preheater.<br />

77.* Can you believe that 0.800 kg/s of air at 60.0°C and1.50<br />

MPa is mixed in an open heat exchanger with 1.50 kg/s of<br />

air at 20.0°C and 1.50 MPa to produce an outlet mixture at<br />

30.0°C at 1.50 MPa? Determine the second law availability<br />

efficiency of this heat exchanger. Neglect all kinetic and<br />

potential energy effects, and take the local environment<br />

(ground state) to be 0.101 MPa and 20.0°C.<br />

78.* A student is using a bathtub with separate hot and cold water<br />

faucets. The student turns on both faucets and adjusts them to<br />

create a pool of warm water in the tub. The tub’s drain is<br />

open, so the faucets must be kept running to maintain the<br />

pool of water. The hot water faucet provides 40.0°C water at<br />

0.100 kg/s, and the cold water faucet provides 15.0°C water at<br />

0.250 kg/s. The local environment (ground state) is at 0.101<br />

MPa and 18.0°C. Neglecting all flow stream kinetic and<br />

potential energy and assuming the tub itself is insulated,<br />

determine<br />

a. The temperature of the mixed water in the tub.<br />

b. The second law availability efficiency of the tub as a<br />

mixing type heat exchanger.<br />

Design Problems<br />

The following are open-ended design problems. The objective is to<br />

carry out a preliminary thermal design as indicated. A detailed design<br />

with working drawings is not required unless otherwise specified by<br />

your instructor. These problems do not have specific answers, so each<br />

student’s design is unique.<br />

79.* Carry out the preliminary design of a closed domestic hot<br />

water heater that has a first law efficiency of at least 95.0%<br />

and a second law efficiency of at least 10.0%. The inlet water<br />

temperature is fixed at 10.0°C. The remaining variables<br />

(including the ground state) are unrestrained and can be<br />

chosen to fit the needs of the designer.<br />

80. You are to prepare the preliminary design of a commercial,<br />

open, liquid water heater that has a first law efficiency of at<br />

least 88.0% and a second law efficiency of at least 15.0%. The<br />

inlet water temperature is fixed at 50.0°F. The remaining<br />

variables (including the ground state) are unrestrained and can<br />

be chosen to fit the needs of the designer.<br />

81.* As chief engineer of a large heat exchanger company, you are<br />

to prepare the preliminary design of a nonmixing heat<br />

exchanger that has a second law availability efficiency of at<br />

least 15.0%. The two flow streams are to be liquid water,<br />

with one flow stream having a mass flow rate of 10 kg/s,<br />

entering at 10.0°C and leaving at 30.0°C. The remaining<br />

variables (including the ground state) are not specified and<br />

are left to the discretion of the designer.<br />

82. Design a benchtop apparatus that illustrates the basic<br />

principles of a mixing heat exchanger. You may use either<br />

liquids or gases or a combination of liquids and gases as the<br />

flow streams. Determine the measurements that must be made<br />

to compute the second law availability of the heat exchanger.<br />

83. Carry out the preliminary design of an instrument that<br />

provides a readout of the specific availability of any fluid<br />

(liquid or gas) in which it is immersed. Determine the<br />

necessary sensors and any calibration procedure required.<br />

Computer Problems<br />

The following open-ended computer problems are designed to be<br />

done on a personal computer using a spreadsheet or equation solver.<br />

84. Plot the specific availability of the air in the tank in Example<br />

10.2 as a function of air pressure. Assume all the remaining<br />

variables are constant.

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