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Modern Engineering Thermodynamics

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246 CHAPTER 7: Second Law of <strong>Thermodynamics</strong> and Entropy Transport and Production Mechanisms<br />

37. Determine the work mode (a) entropy transport rate and<br />

(b) entropy production rate as 100. hp is continuously dissipated<br />

in a mechanical brake operating isothermally at 300.°F.<br />

38.* Determine the work mode entropy production as a 300. kg steel<br />

block slides 10.0 m down a 60.0° incline. The coefficient of<br />

friction between the block and the incline is 0.100, and the bulk<br />

mean temperature of the sliding surface is 50.0°C.<br />

39. A mechanical gearbox at a uniform temperature of 160.°F<br />

receives 150. hp at the input shaft and transmits 145 hp out the<br />

output shaft. Determine its work mode (a) entropy transport<br />

rate and (b) entropy production rate.<br />

40.* Determine the work mode entropy production as 0.500 m 3<br />

of air is compressed adiabatically from 200. kPa, 20.0°C to<br />

0.100 m 3 in a piston-cylinder apparatus with a mechanical<br />

efficiency of 85.0%. Assume constant specific heat ideal gas<br />

behavior.<br />

41. The velocity profile for the steady laminar flow of an<br />

incompressible Newtonian fluid in a horizontal circular pipe<br />

(Figure 7.27) is<br />

V = V max ½1 − ðx/RÞ 2 Š<br />

where V max is the centerline (x = 0) velocity, R is the pipe radius,<br />

and x is the radial coordinate measured from the centerline.<br />

a. Determine the position in this flow where the entropy<br />

production rate per unit volume is a minimum.<br />

b. Determine the position in this flow where the entropy<br />

production rate per unit volume is a maximum.<br />

c. Comment on how you can minimize the total entropy<br />

production rate for this flow.<br />

C L<br />

FIGURE 7.27<br />

Problem 41.<br />

42. The viscous work entropy production rate per unit volume in<br />

three-dimensional Cartesian coordinates is<br />

( "<br />

ðσ W Þ vis<br />

= μ <br />

2 ∂V x<br />

T 3 ∂x − ∂V 2 <br />

y<br />

+ ∂V y<br />

∂y ∂y − ∂V #<br />

2 <br />

z<br />

+ ∂V z<br />

∂z ∂z − ∂V 2<br />

x<br />

∂x<br />

<br />

+ ∂V x<br />

∂y + ∂V 2<br />

y<br />

+ ∂V y<br />

∂x<br />

R<br />

x<br />

<br />

∂z + ∂V 2<br />

z<br />

+ ∂V z<br />

∂y<br />

V m<br />

)<br />

<br />

∂x + ∂V 2<br />

x<br />

∂z<br />

Show that this can be written as<br />

(<br />

ðσ W Þ vis = μ − 2 <br />

∂V x<br />

T 3 ∂x + ∂V y<br />

∂y + ∂V 2<br />

z<br />

∂z<br />

"<br />

<br />

∂V 2<br />

#<br />

+ 2 x<br />

∂V 2 y<br />

+ + ∂V 2<br />

z<br />

∂x ∂y ∂z<br />

<br />

+ ∂V x<br />

∂y + ∂V 2 <br />

y<br />

+ ∂V y<br />

∂x ∂z + ∂V )<br />

2 <br />

z<br />

+ ∂V z<br />

∂y ∂x + ∂V 2<br />

x<br />

∂z<br />

43. Show that the three-dimensional Cartesian coordinate viscous<br />

work entropy production rate per unit volume given in Problem<br />

42 reduces to the following for two-dimensional incompressible<br />

flow:<br />

ðσ W Þ vis = μ <br />

∂V x<br />

T ∂y + ∂V 2<br />

y<br />

∂x<br />

<br />

Hint: For incompressible fluids, ∂V x<br />

∂x + ∂V y<br />

∂y + ∂V <br />

z<br />

∂z = 0:<br />

44.* Determine the entropy production rate of a 10.0 × 10 3 Ω<br />

electrical resistor that draws a constant 10.0 mA of current. The<br />

temperature of the resistor is constant throughout its volume at<br />

35.0°C.<br />

Computer Problems<br />

The following computer programming assignments are designed to<br />

be carried out on any personal computer using a spreadsheet or<br />

equation solver. They are meant to be exercises in the manipulation<br />

of some of the basic formulae of this chapter. They may be used as<br />

part of a weekly homework assignment.<br />

45. Develop a program that allows you to input any temperature<br />

(i.e., value plus unit symbol) in either the relative or absolute<br />

<strong>Engineering</strong> English or SI units system at the keyboard and<br />

converts this input into all the following temperatures and<br />

outputs them to the screen:<br />

°C, °F, R, and K.<br />

46. Develop a program that computes the change in specific internal<br />

energy, enthalpy, and entropy for an incompressible material.<br />

Input the initial and final temperatures and pressures, the<br />

specific heat, and the specific volume or density of the material.<br />

Output u 1 − u 2 , h 2 − h 1 , and s 2 − s 1 to the screen along with<br />

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

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

47. Develop a program that computes the change in specific internal<br />

energy, enthalpy, and entropy for a constant specific heat ideal<br />

gas. Input the initial and final temperatures and pressures or<br />

specific volumes (allow the user the choice of which to input),<br />

the specific heats and gas constant. Output u 2 − u 1 , h 2 − h 1 , and<br />

s 2 − s 1 to the screen along with their proper units. Allow the<br />

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

SI units system.<br />

48. Repeat Problem 47 except allow the user to choose a gas from a<br />

menu. Have all the specific heats and gas constants for the gases<br />

resident in your program.<br />

49. Develop a program that outputs the heat production rate ð_S P Þ Q<br />

of entropy due to steady state, one-dimensional thermal<br />

conduction. Utilize Fourier’s law of conduction and input the<br />

appropriate temperatures, thermal conductivity, cross-sectional<br />

area, and length in the proper units. Allow the choice of<br />

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

system.<br />

50. Develop a program that outputs the work mode entropy<br />

production rate _S P due to the viscous dissipation in the<br />

w<br />

steady one-dimensional flow of a Newtonian fluid in a circular<br />

pipe with the velocity profile given in Problem 41. Input the<br />

fluid’s viscosity, density, and mass flow rate and the appropriate<br />

pipe dimensions in proper units. Allow the choice of working in<br />

either the <strong>Engineering</strong> English or the SI units system.

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