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Modern Engineering Thermodynamics

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Problems 317<br />

The cavitation process is the formation of these vapor bubbles.<br />

Carry out the preliminary thermodynamic design of a closed<br />

loop apparatus that illustrates this phenomenon by having a<br />

liquid pumped through a transparent nozzle wherein the<br />

pressure drops below the local saturation pressure and the<br />

vapor bubbles become visible. Choose a suitable liquid and<br />

provide an engineering sketch containing all the major<br />

dimensions and materials of your system. Estimate the pump<br />

size and power required, and the entropy production rate of<br />

your nozzle.<br />

73. The Engine Test Facility at the Arnold Air Force Base in Tennessee<br />

requires a test cell 48.0 ft in diameter and 85.0 ft long with an air<br />

flow rate of 4300. ft 3 /s at atmospheric pressure and temperature.<br />

Carry out the preliminary thermodynamic design of a<br />

compressor-nozzle system that meets these requirements. The<br />

compressor inlet is at atmospheric conditions, and the inlet<br />

temperature of the nozzle must be 70.0°F (this means an<br />

intercooling system must be used). Determine the horsepower<br />

required to drive the compressor, the nozzle outlet temperature,<br />

and the entropy production rate of your nozzle. Assume the<br />

compression process is polytropic with n = 1.30 and the pressure<br />

loss through the nozzle is 15.0% of the inlet pressure.<br />

74. The Aeropropulsion System Test Facility at the Arnold Air Force<br />

Base in Tennessee requires a heat exchanger capable of cooling<br />

2750. lbm/s of gas turbine exhaust from 3500. to 80.0°F before<br />

discharging it to the atmosphere. Carry out a preliminary<br />

thermodynamic design of a suitable heat exchanger using water<br />

as the second fluid. Determine the amount of cooling water<br />

needed and recommend an appropriate source. Also determine<br />

the entropy production rate of your heat exchanger.<br />

75.* Carry out the preliminary thermodynamic design of a fuel<br />

mixing valve for a furnace that efficiently mixes inlet flow<br />

streams of air at 2.50 kg/s and methane at 0.500 kg/s, both at<br />

atmospheric pressure and temperature, and produces one outlet<br />

flow stream. Assume these gases behave as constant specific heat<br />

ideal gases. Provide a dimensioned engineering sketch and<br />

estimate the entropy production rate of your valve.<br />

76.* Carry out the preliminary thermodynamic design of a system<br />

that uses a vortex tube to cool a full body suit for a firefighter.<br />

The suit must be able to reject up to 1300. kJ/h, and this<br />

cooling rate must be easily adjustable by the wearer. Use the<br />

data given in Case Study 9.1 or from appropriate industrial<br />

literature.<br />

77. Carry out the preliminary thermodynamic design of a system<br />

that uses a vortex tube to heat a skintight suit for an underwater<br />

diver by bleeding off part of the air supply to the diver. The suit<br />

must be able to supply 800. Btu/h, and this heating rate must<br />

be easily adjustable by the diver. Use the data given in Case<br />

Study 9.1 or from appropriate industrial literature.<br />

78.* Carry out the preliminary thermodynamic design of a system that<br />

isothermally fills an initially evacuated, rigid, cylindrical tank with<br />

air at 20.0°C to 20.0 MPa with a minimum amount of entropy<br />

production. The tank is 0.250 m in diameter and 1.50 m high.<br />

Assume the air behaves as a constant specific heat ideal gas.<br />

Discuss the technology and economics of how the tank is<br />

maintained isothermal during the filling process. Note that there<br />

will beentropy production in the pipes and valves used to connect<br />

the tank to the air supply.<br />

79. The Von Karman Gas Dynamics Facility at the Arnold Air Force<br />

Base in Tennessee has need of a blowdown wind tunnel, to be<br />

supplied from a tank containing compressed air initially at<br />

1000. psia and 70.0°F. The wind tunnel is to be at the end of<br />

a nozzle attached to the tank and must be 8.00 ft in diameter<br />

and have a velocity of 10.0 × 10 3 ft/s at 2000. R. The tank must<br />

be of sufficient size to sustain these wind tunnel conditions for<br />

a minimum of 30.0 min of testing. Carry out the preliminary<br />

thermodynamic design of such a facility and estimate the size of<br />

the storage tank required and the power required to compress the<br />

air in filling the tank if it must be done overnight (i.e., in 8.00 h).<br />

Determine the entropy production associated with both the filling<br />

and emptying of the tank if both are done isothermally.<br />

Computer problems<br />

The following computer assignments are designed to be carried out<br />

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

are meant to be exercises using some of the basic formulae of<br />

this chapter. They may be used as part of a weekly homework<br />

assignment.<br />

80.* Develop a program that allows you to plot the entropy<br />

production rate discussed in Example 9.1 vs. the heat transfer<br />

rate. Let the heat transfer rate range from 100. to 1000. watts.<br />

Assume all the remaining variables are as given in Example 9.1.<br />

81. Develop a program that determines the entropy production rate<br />

of an incompressible fluid or a constant specific heat ideal gas<br />

of your choice flowing through an adiabatic nozzle. Input all<br />

the variables with proper units. Allow the choice of working in<br />

either <strong>Engineering</strong> English or SI units.<br />

82. Develop a program that determines the entropy production rate<br />

of an incompressible fluid or constant specific heat ideal gas of<br />

your choice from an adiabatic diffuser. Input all the variables<br />

with proper units. Allow the choice of working in either<br />

<strong>Engineering</strong> English or SI units.<br />

83. Develop a program that determines the entropy production<br />

inside a heat exchanger having two inlets and two outlets, when<br />

the mass flow rates, temperatures, and fluid properties of both of<br />

the flow stream fluids are known. Assume the fluids do not mix<br />

inside the heat exchanger, and allow either flow stream to be an<br />

incompressible liquid or a constant specific heat ideal gas at the<br />

user’s discretion. Input all the variables with proper units. Allow<br />

the choice of working in either <strong>Engineering</strong> English or SI units.<br />

84. Develop a program that performs an energy rate balance on a<br />

gas turbine engine. Input the appropriate gas properties (in the<br />

proper units), the turbine’s heat loss or gain rate, and the input<br />

mass flow rate, and the inlet and exit temperatures. Output to<br />

the screen the turbine’s output power. Assume the gas behaves<br />

as a constant specific heat ideal gas, and neglect all kinetic and<br />

potential energy terms. Allow the choice of working in either<br />

<strong>Engineering</strong> English or SI units.<br />

85. Curve fit the hot and cold vortex tube outlet temperature data<br />

given in Case Study 9.1 vs. the inlet absolute pressure. Then<br />

develop a program that returns these outlet temperatures plus<br />

the COP of this device when it is used as a Carnot heat pump<br />

and when it is used as a Carnot refrigerator or air conditioner<br />

when the user inputs the inlet pressure. Use this program to<br />

generate enough data to plot the values of these two COPs vs.<br />

the inlet absolute pressure.<br />

86. Develop a program that outputs the entropy production rate for<br />

the filling of an initially evacuated rigid vessel with an

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