fluid_mechanics
xvi Featured in this Book STUDENT SOLUTION MANUAL AND STUDY GUIDE A brief paperback book titled Student Solution Manual and Study Guide for Fundamentals of Fluid Mechanics, by Munson, et al. (© 2009 John Wiley and Sons, Inc.), is available. It contains detailed solutions to the Review Problems and a study guide with a brief summary and sample problems with solutions for most major sections of the book. 5.118 Water flows by gravity from one lake to another as sketched in Fig. P5.118 at the steady rate of 80 gpm. What is the loss in available energy associated with this flow? If this same amount of loss is associated with pumping the fluid from the lower lake to the higher one at the same flowrate, estimate the amount of pumping power required. 8-in. insidediameter pipe Section (2) 50 ft Section (1) Pump 50 ft F I G U R E P5.121 HOMEWORK PROBLEMS Homework problems at the end of each chapter stress the practical applications of fluid mechanics principles. Over 1350 homework problems are included. energy associated with 2.5 ft 3 s being pumped from sections 112 to F I G U R E P5.118 122 is loss 61V 2 2 ft 2 s 2 , where V is the average velocity of water in the 8-in. inside diameter piping involved. Determine the 5.119 Water is pumped from a tank, point (1), to the top of a water plant aerator, point (2), as shown in Video V5.14 and Fig. amount of shaft power required. P5.119 at a rate of 3.0 ft 3 5.122 Water is to be pumped from the large tank shown in Fig. /s. (a) Determine the power that the pump P5.122 with an exit velocity of 6 ms. It was determined that the adds to the water if the head loss from (1) to (2) where V 2 0 is 4 ft. original pump (pump 1) that supplies 1 kW of power to the water (b) Determine the head loss from (2) to the bottom of the aerator did not produce the desired velocity. Hence, it is proposed that an column, point (3), if the average velocity at (3) is V 3 2 ft/s. additional pump (pump 2) be installed as indicated to increase the flowrate to the desired value. How much power must pump 2 add to Aerator column (2) the water? The head loss for this flow is h L 250Q 2 , where h L is in m when Q is in m 3 s. 10 ft (1) Nozzle area = 0.01 m 2 Pipe area = 0.02 m 2 V = 6 m/s Pump Pump #2 #1 2 m (3) 5 ft 3 ft F I G U R E P5.122 Pump 5.123 (See Fluids in the News article titled “Curtain of air,” Section 5.3.3.) The fan shown in Fig. P5.123 produces an air curtain to F I G U R E P5.119 separate a loading dock from a cold storage room. The air curtain is 5.120 A liquid enters a fluid machine at section 112 and leaves at a jet of air 10 ft wide, 0.5 ft thick moving with speed V 30 fts. The sections 122 and 132 as shown in Fig. P5.120. The density of the fluid loss associated with this flow is loss K LV 2 2, where K L 5. How is constant at 2 slugsft 3 . All of the flow occurs in a horizontal plane much power must the fan supply to the air to produce this flow? and is frictionless and adiabatic. For the above-mentioned and additional conditions indicated in Fig. P5.120, determine the amount of shaft power involved. Fan Section (2) p 2 = 50 psia V 2 = 35 ft/s 10 ft V = 30 ft/s Air curtain (0.5-ft thickness) Open door Section (3) F I G U R E P5.123 p 1 = 80 psia V 1 = 15 ft/s A 1 = 30 in. 2 Section (1) F I G U R E P5.120 p 3 = 14.7 psia V 3 = 45 ft/s A 3 = 5 in. 2 5.121 Water is to be moved from one large reservoir to another at a higher elevation as indicated in Fig. P5.121. The loss of available Section 5.3.2 Application of the Energy Equation— Combined with Linear momentum 3 5.124 If a 4-hp motor is required by a ventilating fan to produce a 24-in. stream of air having a velocity of 40 ft/s as shown in Fig. P5.124, estimate (a) the efficiency of the fan and (b) the thrust of the supporting member on the conduit enclosing the fan. 5.125 Air flows past an object in a pipe of 2-m diameter and exits as a free jet as shown in Fig. P5.125. The velocity and pressure upstream are uniform at 10 ms and 50 Nm 2 , respectively. At the Axial Velocity Axial Velocity (m/s) 0.0442 0.0395 0.0347 Legend inlet x = 0.5d x = 1d x = 5d x = 10d x = 25d outlet 0.03 0.0253 0.0205 0.0158 0.0111 0.00631 0.00157 0 Position (n) Full XLog YLog Symbols Lines X Grid Y Grid Legend Manager Done Legend Freeze Auto Raise Print 0.1 Export Data CFD FlowLab For those who wish to become familiar with the basic concepts of computational fluid dynamics, a new overview to CFD is provided in Appendices A and I. In addition, the use of FlowLab software to solve interesting flow problems is described in Appendices J and K.
C ontents 1 INTRODUCTION 1 Learning Objectives 1 1.1 Some Characteristics of Fluids 3 1.2 Dimensions, Dimensional Homogeneity, and Units 4 1.2.1 Systems of Units 7 1.3 Analysis of Fluid Behavior 11 1.4 Measures of Fluid Mass and Weight 11 1.4.1 Density 11 1.4.2 Specific Weight 12 1.4.3 Specific Gravity 12 1.5 Ideal Gas Law 12 1.6 Viscosity 14 1.7 Compressibility of Fluids 20 1.7.1 Bulk Modulus 20 1.7.2 Compression and Expansion of Gases 21 1.7.3 Speed of Sound 22 1.8 Vapor Pressure 23 1.9 Surface Tension 24 1.10 A Brief Look Back in History 27 1.11 Chapter Summary and Study Guide 29 References 30 Review Problems 30 Problems 31 2 FLUID STATICS 38 Learning Objectives 38 2.1 Pressure at a Point 38 2.2 Basic Equation for Pressure Field 40 2.3 Pressure Variation in a Fluid at Rest 41 2.3.1 Incompressible Fluid 42 2.3.2 Compressible Fluid 45 2.4 Standard Atmosphere 47 2.5 Measurement of Pressure 48 2.6 Manometry 50 2.6.1 Piezometer Tube 50 2.6.2 U-Tube Manometer 51 2.6.3 Inclined-Tube Manometer 54 2.7 Mechanical and Electronic Pressure Measuring Devices 55 2.8 Hydrostatic Force on a Plane Surface 57 2.9 Pressure Prism 63 2.10 Hydrostatic Force on a Curved Surface 66 2.11 Buoyancy, Flotation, and Stability 68 2.11.1 Archimedes’ Principle 68 2.11.2 Stability 71 2.12 Pressure Variation in a Fluid with Rigid-Body Motion 72 2.12.1 Linear Motion 73 2.12.2 Rigid-Body Rotation 75 2.13 Chapter Summary and Study Guide 77 References 78 Review Problems 78 Problems 78 3 ELEMENTARY FLUID DYNAMICS—THE BERNOULLI EQUATION 93 Learning Objectives 93 3.1 Newton’s Second Law 94 3.2 F ma along a Streamline 96 3.3 F ma Normal to a Streamline 100 3.4 Physical Interpretation 102 3.5 Static, Stagnation, Dynamic, and Total Pressure 105 3.6 Examples of Use of the Bernoulli Equation 110 3.6.1 Free Jets 110 3.6.2 Confined Flows 112 3.6.3 Flowrate Measurement 118 3.7 The Energy Line and the Hydraulic Grade Line 123 3.8 Restrictions on Use of the Bernoulli Equation 126 3.8.1 Compressibility Effects 126 3.8.2 Unsteady Effects 128 3.8.3 Rotational Effects 130 3.8.4 Other Restrictions 131 3.9 Chapter Summary and Study Guide 131 References 133 Review Problems 133 Problems 133 xvii
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xvi<br />
Featured in this Book<br />
STUDENT SOLUTION MANUAL AND STUDY GUIDE<br />
A brief paperback book titled Student Solution Manual and<br />
Study Guide for Fundamentals of Fluid Mechanics, by<br />
Munson, et al. (© 2009 John Wiley and Sons, Inc.), is<br />
available. It contains detailed solutions to the Review<br />
Problems and a study guide with a brief summary and<br />
sample problems with solutions for most major sections of<br />
the book.<br />
5.118 Water flows by gravity from one lake to another as sketched in<br />
Fig. P5.118 at the steady rate of 80 gpm. What is the loss in available<br />
energy associated with this flow? If this same amount of loss is associated<br />
with pumping the <strong>fluid</strong> from the lower lake to the higher one at<br />
the same flowrate, estimate the amount of pumping power required.<br />
8-in. insidediameter<br />
pipe<br />
Section (2)<br />
50 ft<br />
Section (1)<br />
Pump<br />
50 ft<br />
F I G U R E P5.121<br />
HOMEWORK PROBLEMS<br />
Homework problems at the end<br />
of each chapter stress the practical<br />
applications of <strong>fluid</strong><br />
<strong>mechanics</strong> principles. Over<br />
1350 homework problems are<br />
included.<br />
energy associated with 2.5 ft 3 s being pumped from sections 112 to<br />
F I G U R E P5.118<br />
122 is loss 61V 2 2 ft 2 s 2 , where V is the average velocity of water<br />
in the 8-in. inside diameter piping involved. Determine the<br />
5.119 Water is pumped from a tank, point (1), to the top of a water<br />
plant aerator, point (2), as shown in Video V5.14 and Fig.<br />
amount of shaft power required.<br />
P5.119 at a rate of 3.0 ft 3 5.122 Water is to be pumped from the large tank shown in Fig.<br />
/s. (a) Determine the power that the pump<br />
P5.122 with an exit velocity of 6 ms. It was determined that the<br />
adds to the water if the head loss from (1) to (2) where V 2 0 is 4 ft.<br />
original pump (pump 1) that supplies 1 kW of power to the water<br />
(b) Determine the head loss from (2) to the bottom of the aerator<br />
did not produce the desired velocity. Hence, it is proposed that an<br />
column, point (3), if the average velocity at (3) is V 3 2 ft/s.<br />
additional pump (pump 2) be installed as indicated to increase the<br />
flowrate to the desired value. How much power must pump 2 add to<br />
Aerator column<br />
(2)<br />
the water? The head loss for this flow is h L 250Q 2 , where h L is in<br />
m when Q is in m 3 s.<br />
10 ft<br />
(1)<br />
Nozzle area = 0.01 m 2<br />
Pipe area = 0.02 m 2<br />
V = 6 m/s<br />
Pump<br />
Pump<br />
#2<br />
#1<br />
2 m<br />
(3)<br />
5 ft<br />
3 ft<br />
F I G U R E P5.122<br />
Pump<br />
5.123 (See Fluids in the News article titled “Curtain of air,” Section<br />
5.3.3.) The fan shown in Fig. P5.123 produces an air curtain to<br />
F I G U R E P5.119<br />
separate a loading dock from a cold storage room. The air curtain is<br />
5.120 A liquid enters a <strong>fluid</strong> machine at section 112 and leaves at a jet of air 10 ft wide, 0.5 ft thick moving with speed V 30 fts. The<br />
sections 122 and 132 as shown in Fig. P5.120. The density of the <strong>fluid</strong> loss associated with this flow is loss K LV 2 2, where K L 5. How<br />
is constant at 2 slugsft 3 . All of the flow occurs in a horizontal plane much power must the fan supply to the air to produce this flow?<br />
and is frictionless and adiabatic. For the above-mentioned and additional<br />
conditions indicated in Fig. P5.120, determine the amount<br />
of shaft power involved.<br />
Fan<br />
Section (2)<br />
p 2 = 50 psia<br />
V 2 = 35 ft/s<br />
10 ft<br />
V = 30 ft/s<br />
Air curtain<br />
(0.5-ft thickness)<br />
Open door<br />
Section (3)<br />
F I G U R E P5.123<br />
p 1 = 80 psia<br />
V 1 = 15 ft/s<br />
A 1 = 30 in. 2<br />
Section (1)<br />
F I G U R E P5.120<br />
p 3 = 14.7 psia<br />
V 3 = 45 ft/s<br />
A 3 = 5 in. 2<br />
5.121 Water is to be moved from one large reservoir to another at<br />
a higher elevation as indicated in Fig. P5.121. The loss of available<br />
Section 5.3.2 Application of the Energy Equation—<br />
Combined with Linear momentum<br />
3<br />
5.124 If a 4-hp motor is required by a ventilating fan to produce a<br />
24-in. stream of air having a velocity of 40 ft/s as shown in<br />
Fig. P5.124, estimate (a) the efficiency of the fan and (b) the thrust<br />
of the supporting member on the conduit enclosing the fan.<br />
5.125 Air flows past an object in a pipe of 2-m diameter and exits<br />
as a free jet as shown in Fig. P5.125. The velocity and pressure upstream<br />
are uniform at 10 ms and 50 Nm 2 , respectively. At the<br />
Axial Velocity<br />
Axial Velocity (m/s)<br />
0.0442<br />
0.0395<br />
0.0347<br />
Legend<br />
inlet<br />
x = 0.5d<br />
x = 1d<br />
x = 5d<br />
x = 10d<br />
x = 25d<br />
outlet<br />
0.03<br />
0.0253<br />
0.0205<br />
0.0158<br />
0.0111<br />
0.00631<br />
0.00157<br />
0<br />
Position (n)<br />
Full<br />
XLog YLog Symbols Lines X Grid Y Grid Legend Manager<br />
Done Legend Freeze<br />
Auto Raise<br />
Print<br />
0.1<br />
Export Data<br />
CFD FlowLab<br />
For those who wish to become familiar with the<br />
basic concepts of computational <strong>fluid</strong> dynamics, a<br />
new overview to CFD is provided in Appendices<br />
A and I. In addition, the use of FlowLab software<br />
to solve interesting flow problems is described in<br />
Appendices J and K.