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Modern Engineering Thermodynamics

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Problems 277<br />

46. a. Determine a formula for the final pressure (p 2 )thatresults<br />

when two volumes of the same constant specific heat ideal<br />

gas initially at p a , T a and p b , T b are mixed isentropically.<br />

b. Does this mixture pressure represent an upper or lower<br />

bound when this mixing is done adiabatically but not<br />

isentropically?<br />

47. Determine the entropy produced as 5.0 × 10 –3 lbm of human<br />

saliva at 98.6°F is adiabatically mixed with 3.00 × 10 –3 lbm of<br />

human saliva at 103.2°F in a passionate and infectious kiss. The<br />

specific heat of the saliva is 0.950 Btu/(lbm·R).<br />

48.* Determine the entropy produced as 10.0 kg of liquid water at<br />

10.0°C is adiabatically mixed with 20.0 kg of liquid water at<br />

80.0°C. The specific heat of the water is 4.20 kJ/(kg·K).<br />

49. Here is the complete classical coffee and cream problem. Which<br />

of the following processes produces less entropy:<br />

a. Mixing cream with hot coffee and letting the mixture cool to<br />

the drinking temperature.<br />

b. Letting the coffee cool to a temperature such that, when the<br />

cream is added, the mixture will be at the drinking<br />

temperature? Do not ignore the cooling heat transfer entropy<br />

production.<br />

Design Problems<br />

The following are elementary, open-ended design problems. The<br />

objective is to carry out a preliminary thermal design as indicated.<br />

A detailed design with working drawings is not expected unless<br />

otherwise specified. These problems do not have specific answers,<br />

so each student’s design is unique.<br />

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

heats 20.0 kg of liquid water from 20.0 to 80.0°C in 15.0 min<br />

at atmospheric pressure in a closed vessel. Use an electrical<br />

heating system and determine the electrical power and current<br />

requirements (assume standard line voltage values). Include a<br />

means of relieving any pressure buildup, and discuss safety<br />

considerations.<br />

51. Carry out a preliminary thermodynamic design of a single<br />

piston-cylinder apparatus that produces 25.0 hp as it moves<br />

through a mechanical cycle in 10.0 s. The piston is to be<br />

drawn into the cylinder by condensing steam that enters the<br />

apparatusasasaturatedvaporat212°F. No work is done<br />

during the return stroke of the piston, during which time a<br />

fresh charge of steam is drawn into the apparatus. Continuous<br />

motion of this type can be accomplished through the use of a<br />

flywheel.<br />

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

mixes by only diffusive processes 5.00 kg of gaseous CO 2 with<br />

10.0 kg of air in a maximum of 6.00 min in a closed, rigid<br />

vessel. Specify the vessel material, size, and internal geometry<br />

and discuss any relevant safety considerations.<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 />

53. Develop a program that determines the power output from<br />

a reversible solar power plant similar to that discussed in<br />

Example 8.2. Input all the relevant variables (in proper units),<br />

and output the net reversible electrical power produced. At<br />

your instructor’s discretion, add screen graphics depicting<br />

a diagram of the power plant and the input and output<br />

variables. Allow the choice of working in either <strong>Engineering</strong><br />

English or SI units.<br />

54. Develop a program that performs an energy and entropy<br />

balance on a closed system with an isothermal boundary. The<br />

system contains an incompressible substance (either a liquid<br />

or a solid) that is undergoing an irreversible process. Input (in<br />

proper units) the heat and work transports of energy, the<br />

system volume, the initial internal temperature and the<br />

isothermal boundary temperature of the system, and the<br />

density and specific heat of the incompressible material<br />

contained in the system. Output to the screen the system<br />

mass, final temperature, and entropy production. Note that, if<br />

the entropy production becomes negative (an impossible<br />

physical situation), then the system boundary temperature was<br />

not properly specified. Check for this possibility and prompt<br />

the user for another boundary temperature if it occurs.<br />

Allow the choice of working in either <strong>Engineering</strong> English<br />

or SI units.<br />

55. Develop a program that performs an energy and an entropy<br />

balance on a closed system with an isothermal boundary. The<br />

system contains an ideal gas with constant specific heats that is<br />

undergoing an irreversible process. Input (in proper units): the<br />

heat and work transports of energy, the system volume, the<br />

initial temperature and pressure of the system, and the<br />

constant volume specific heat and gas constant of the gas<br />

contained in the system. Output to the screen the system mass,<br />

the final pressure and temperature, and the entropy production<br />

for the process. Check to make sure the entropy production is<br />

positive and prompt the user for corrected input if it is not. Allow<br />

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

56. Repeat Problem 55, except allow the user to choose the system<br />

ideal gas from a screen menu and omit the prompts for gas<br />

properties. Use the data in Table C.13 of Thermodynamic Tables to<br />

accompany <strong>Modern</strong> <strong>Engineering</strong> <strong>Thermodynamics</strong> for the properties<br />

of the gases in your menu.<br />

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

production rate due to the heat transfer from the fin in<br />

Example 8.12 vs. the base temperature of the fin T f .Allow<br />

the T f to range from 20.0 to 200.°C. Keep all the remaining<br />

variables constant.<br />

58.* The temperature profile for the fin discussed in Example 8.12 is<br />

for a “very long” (i.e., infinite) fin. A more accurate equation for<br />

a finite fin of length L is<br />

<br />

<br />

cosh½mðL − xÞŠ + ½h/ðmkÞŠ sinh½mðL − xÞŠ<br />

TðxÞ = T ∞ + ðT f − T ∞ Þ<br />

coshðmLÞ + ½h/ðmkÞŠ sinhðmLÞ<br />

where the remaining variables are defined in Example 8.12.<br />

Using this temperature profile, rework Example 8.12 and<br />

Problem 57 to produce a new plot of entropy production rate vs.<br />

fin base temperature (you may wish to use a numerical

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