Cantitate/Preț
Produs
Total produse
Vezi coșul
Pipe Flow: A Practical and Comprehensive Guide, 2nd Edition de D Rennels

Pipe Flow: A Practical and Comprehensive Guide, 2nd Edition

Autor D Rennels
en Limba Engleză Hardback – 26 mai 2022
Provides detailed coverage of hydraulic analysis of piping systems, revised and updated throughout Pipe Flow: A Practical and Comprehensive Guide provides the information required to design and analyze of piping systems for distribution systems, power plants, and other industrial operations. Divided into three parts, this authoritative resource describes the methodology for solving pipe flow problems, presents loss coefficient data for a wide range of piping components, and examines pressure drop, cavitation, flow-induced vibration, and other flow phenomena that affect the performance of piping systems. Throughout the book, sample problems and worked solutions illustrate the application of core concepts and techniques. The second edition features revised and expanded information throughout, including an entirely new chapter that presents a mixing section flow model for accurately predicting jet pump performance. This edition includes additional examples, supplemental problems, and a new appendix of the speed of sound in water. With clear explanations, expert guidance, and precise hydraulic computations, this classic reference text remains required reading for anyone working to increase the quality and efficiency of modern piping systems. * Discusses the fundamental physical properties of fluids and the nature of fluid flow * Demonstrates the accurate prediction and management of pressure loss for a variety of piping components and piping systems * Reviews theoretical research on fluid flow in piping and its components * Presents important loss coefficient data with straightforward tables, diagrams, and equations * Includes full references, further reading sections, and numerous example problems with solution Pipe Flow: A Practical and Comprehensive Guide, Second Edition is an excellent textbook for engineering students, and an invaluable reference for professional engineers engaged in the design, operation, and troubleshooting of piping systems.
Citește tot Restrânge

Preț: 75144 lei

Preț vechi: 98874 lei
-24% Nou

Puncte Express: 1127
Preț estimativ în valută:
14382€ • 15172$ • 11985£

Carte disponibilă

Livrare economică 12-26 decembrie
Livrare express 27 noiembrie-03 decembrie pentru 5275 lei

 Adaugă în coș

Wish list
Gift list
Am citit!
Adaugă în listă
Preluare comenzi: 021 569.72.76

Specificații

ISBN-13: 9781119756439
ISBN-10: 111975643X
Pagini: 384
Dimensiuni: 218 x 291 x 26 mm
Greutate: 1.16 kg
Ediția:2nd Edition
Editura: Wiley
Locul publicării:Hoboken, United States

Cuprins

Preface to the First Edition xix Preface to the Second Edition xxi Nomenclature xxiii Part I Methodology 1 1 Fundamentals 3 1.1 System of Units 3 1.2 Fluid Properties 4 1.2.1 Pressure 4 1.2.2 Temperature 5 1.2.3 Density 6 1.2.4 Viscosity 6 1.2.5 Energy 7 1.2.6 Heat 7 1.3 Velocity 8 1.4 Important Dimensionless Ratios 8 1.4.1 Reynolds Number 8 1.4.2 Relative Roughness 9 1.4.3 Loss Coefficient 9 1.4.4 Mach Number 9 1.4.5 Froude Number 9 1.4.6 Reduced Pressure 10 1.4.7 Reduced Temperature 10 1.4.8 Ratio of Specific Heats 10 1.5 Equations of State 10 1.5.1 Equation of State of Liquids 10 1.5.2 Equation of State of Gases 11 1.5.3 Two-Phase Mixtures 11 1.6 Flow Regimes 12 1.7 Similarity 12 1.7.1 The Principle of Similarity 12 1.7.2 Limitations 13 References 13 Further Reading 13 2 Conservation Equations 15 2.1 Conservation of Mass 15 2.2 Conservation of Momentum 15 2.3 The Momentum Flux Correction Factor 17 2.4 Conservation of Energy 18 2.4.1 Potential Energy 18 2.4.2 Pressure Energy 19 2.4.3 Kinetic Energy 19 2.4.4 Heat Energy 19 2.4.5 Mechanical Work Energy 20 2.5 General Energy Equation 20 2.6 Head Loss 21 2.7 The Kinetic Energy Correction Factor 21 2.8 Conventional Head Loss 22 2.9 Grade Lines 23 References 23 Further Reading 23 3 Incompressible Flow 25 3.1 Conventional Head Loss 25 3.2 Sources of Head Loss 26 3.2.1 Surface Friction Loss 26 3.2.1.1 Laminar Flow 26 3.2.1.2 Turbulent Flow 26 3.2.1.3 Reynolds Number 27 3.2.1.4 Friction Factor 27 3.2.2 Induced Turbulence 29 3.2.3 Summing Loss Coefficients 31 References 31 Further Reading 32 4 Compressible Flow 33 4.1 Introduction 33 4.2 Problem Solution Methods 34 4.3 Approximate Compressible Flow using Incompressible Flow Equations 34 4.3.1 Using Inlet or Outlet Properties 35 4.3.2 Using Average of Inlet and Outlet Properties 35 4.3.2.1 Simple Average Properties 35 4.3.2.2 Comprehensive Average Properties 36 4.3.3 Using Expansion Factors 37 4.4 Adiabatic Compressible Flow with Friction: Ideal Equations 39 4.4.1 Shapiro's Adiabatic Flow Equation 39 4.4.1.1 Solution when Static Pressure and Static Temperature Are Known 39 4.4.1.2 Solution when Static Pressure and Total Temperature Are Known 41 4.4.1.3 Solution when Total Pressure and Total Temperature Are Known 41 4.4.1.4 Solution when Total Pressure and Static Temperature Are Known 42 4.4.2 Turton's Adiabatic Flow Equation 42 4.4.3 Binder's Adiabatic Flow Equation 43 4.5 Isothermal Compressible Flow with Friction: Ideal Equation 43 4.6 Isentropic Flow: Treating Changes in Flow Area 44 4.7 Pressure Drop in Valves 45 4.8 Two-Phase Flow 45 4.9 Example Problems: Adiabatic Flow with Friction using Guess Work 45 4.9.1 Solve for p2 and t2 . K, p1 , t1 , and W are Known 46 4.9.1.1 Solve Using Expansion Factor Y 46 4.9.1.2 Solve Using Shapiro's Equation 47 4.9.1.3 Solve Using Binder's Equation 47 4.9.1.4 Solve Using Turton's Equation 47 4.9.2 Solve for W and t2 . K, p1 , t1 , and p2 are Known 48 4.9.2.1 Solve Using Expansion Factor Y 48 4.9.2.2 Solve Using Shapiro's Equation 48 4.9.2.3 Solve Using Binder's Equation 49 4.9.2.4 Solve Using Turton's Equation 49 4.9.3 Observations 49 4.10 Example Problem: Natural Gas Pipeline Flow 50 4.10.1 Ground Rules and Assumptions 50 4.10.2 Input Data 50 4.10.3 Initial Calculations 50 4.10.4 Solution 50 4.10.5 Comparison with Crane's Solutions 51 References 51 Further Reading 51 5 Network Analysis 53 5.1 Coupling Effects 53 5.2 Series Flow 54 5.3 Parallel Flow 54 5.4 Branching Flow 55 5.5 Example Problem: Ring Sparger 56 5.5.1 Ground Rules and Assumptions 56 5.5.2 Input Parameters 57 5.5.3 Initial Calculations 57 5.5.4 Network Flow Equations 57 5.5.4.1 Continuity Equations 57 5.5.4.2 Energy Equations 57 5.5.5 Solution 59 5.6 Example Problem: Core Spray System 59 5.6.1 New, Clean Steel Pipe 60 5.6.1.1 Ground Rules and Assumptions 60 5.6.1.2 Input Parameters 60 5.6.1.3 Initial Calculations 62 5.6.1.4 Adjusted Parameters 62 5.6.1.5 Network Flow Equations 63 5.6.1.6 Solution 63 5.6.2 Moderately Corroded Steel Pipe 64 5.6.2.1 Ground Rules and Assumptions 64 5.6.2.2 Input Parameters 64 5.6.2.3 Adjusted Parameters 64 5.6.2.4 Network Flow Equations 65 5.6.2.5 Solution 65 5.7 Example Problem: Main Steam Line Pressure Drop 65 5.7.1 Ground Rules and Assumptions 65 5.7.2 Input Data 66 5.7.3 Initial Calculations 67 5.7.4 Loss Coefficient Calculations 67 5.7.4.1 Individual Loss Coefficients 67 5.7.4.2 Series Loss Coefficients 68 5.7.5 Pressure Drop Calculations 68 5.7.5.1 Steam Dome to Steam Drum 68 5.7.5.2 Steam Drum to Turbine Stop Valves Pressure Drop 69 5.7.6 Predicted Pressure at Turbine Stop Valves 70 References 70 Further Reading 70 6 Transient Analysis 71 6.1 Methodology 71 6.2 Example Problem: Vessel Drain Times 72 6.2.1 Upright Cylindrical Vessel with Flat Heads 72 6.2.2 Spherical Vessel 73 6.2.3 Upright Cylindrical Vessel with Elliptical Heads 74 6.3 Example Problem: Positive Displacement Pump 75 6.3.1 No Heat Transfer 76 6.3.2 Heat Transfer 76 6.4 Example Problem: Time Step Integration 77 6.4.1 Upright Cylindrical Vessel Drain 77 6.4.1.1 Direct Solution 78 6.4.1.2 Time Step Solution 78 References 78 Further Reading 78 7 Uncertainty 79 7.1 Error Sources 79 7.2 Pressure Drop Uncertainty 81 7.3 Flow Rate Uncertainty 81 7.4 Example Problem: Pressure Drop 81 7.4.1 Input Data 81 7.4.2 Solution 82 7.5 Example Problem: Flow Rate 82 7.5.1 Input Data 83 7.5.2 Solution 83 Further Reading 84 Part II Loss Coefficients 85 8 Surface Friction 87 8.1 Reynolds Number and Surface Roughness 87 8.2 Friction Factor 87 8.2.1 Laminar Flow Region 87 8.2.2 Critical Zone 88 8.2.3 Turbulent Flow Region 88 8.2.3.1 Smooth Pipes 88 8.2.3.2 Rough Pipes 88 8.3 The Colebrook-White Equation 88 8.4 The Moody Chart 89 8.5 Explicit Friction Factor Formulations 89 8.5.1 Moody's Approximate Formula 89 8.5.2 Wood's Approximate Formula 90 8.5.3 The Churchill 1973 and Swamee and Jain Formulas 90 8.5.4 Chen's Formula 90 8.5.5 Shacham's Formula 90 8.5.6 Barr's Formula 90 8.5.7 Haaland's Formulas 90 8.5.8 Manadilli's Formula 90 8.5.9 Romeo's Formula 91 8.5.10 Evaluation of Explicit Alternatives to the Colebrook- White Equation 91 8.6 All-Regime Friction Factor Formulas 91 8.6.1 Churchill's 1977 Formula 91 8.6.2 Modifications to Churchill's 1977 Formula 92 8.7 Absolute Roughness of Flow Surfaces 93 8.8 Age and usage of Pipe 94 8.8.1 Corrosion and Encrustation 95 8.8.2 The Relationship Between Absolute Roughness and Friction Factor 95 8.8.3 Inherent Margin 95 8.9 Noncircular Passages 97 References 97 Further Reading 98 9 Entrances 101 9.1 Sharp-Edged Entrance 101 9.1.1 Flush Mounted 101 9.1.2 Mounted at a Distance 102 9.1.3 Mounted at an Angle 102 9.2 Rounded Entrance 103 9.3 Beveled Entrance 104 9.4 Entrance Through an Orifice 104 9.4.1 Sharp-Edged Orifice 105 9.4.2 Round-Edged Orifice 105 9.4.3 Thick-Edged Orifice 105 9.4.4 Beveled Orifice 106 References 111 Further Reading 111 10 Contractions 113 10.1 Flow Model 113 10.2 Sharp-Edged Contraction 114 10.3 Rounded Contraction 115 10.4 Conical Contraction 116 10.4.1 Surface Friction Loss 117 10.4.2 Local Loss 118 10.5 Beveled Contraction 119 10.6 Smooth Contraction 119 10.7 Pipe Reducer - Contracting 120 References 125 Further Reading 125 11 Expansions 127 11.1 Sudden Expansion 127 11.2 Straight Conical Diffuser 128 11.3 Multi-Stage Conical Diffusers 131 11.3.1 Stepped Conical Diffuser 132 11.3.2 Two-Stage Conical Diffuser 132 11.4 Curved Wall Diffuser 135 11.5 Pipe Reducer - Expanding 136 References 142 Further Reading 142 12 Exits 145 12.1 Discharge from a Straight Pipe 145 12.2 Discharge from a Conical Diffuser 146 12.3 Discharge from an Orifice 146 12.3.1 Sharp-Edged Orifice 147 12.3.2 Round-Edged Orifice 147 12.3.3 Thick-Edged Orifice 147 12.3.4 Bevel-Edged Orifice 148 12.4 Discharge from a Smooth Nozzle 148 13 Orifices 153 13.1 Generalized Flow Model 154 13.2 Sharp-Edged Orifice 155 13.2.1 In a Straight Pipe 155 13.2.2 In a Transition Section 156 13.2.3 In a Wall 157 13.3 Round-Edged Orifice 157 13.3.1 In a Straight Pipe 157 13.3.2 In a Transition Section 158 13.3.3 In a Wall 159 13.4 Bevel-Edged Orifice 159 13.4.1 In a Straight Pipe 159 13.4.2 In a Transition Section 160 13.4.3 In a Wall 160 13.5 Thick-Edged Orifice 161 13.5.1 In a Straight Pipe 161 13.5.2 In a Transition Section 162 13.5.3 In a Wall 163 13.6 Multi-Hole Orifices 163 13.7 Non-Circular Orifices 164 References 169 Further Reading 170 14 Flow Meters 173 14.1 Flow Nozzle 173 14.2 Venturi Tube 174 14.3 Nozzle/Venturi 175 References 177 Further Reading 177 15 Bends 179 15.1 Overview 179 15.2 Bend Losses 180 15.2.1 Smooth-Walled Bends 181 15.2.2 Welded Elbows and Pipe Bends 182 15.3 Coils 185 15.3.1 Constant Pitch Helix 185 15.3.2 Constant Pitch Spiral 185 15.4 Miter Bends 186 15.5 Coupled Bends 187 15.6 Bend Economy 187 References 192 Further Reading 193 16 Tees 195 16.1 Overview 195 16.1.1 Previous Endeavors 195 16.1.2 Observations 197 16.2 Diverging Tees 197 16.2.1 Diverging Flow Through Run 197 16.2.2 Diverging Flow Through Branch 199 16.2.3 Diverging Flow from Branch 202 16.3 Converging Tees 202 16.3.1 Converging Flow Through Run 202 16.3.2 Converging Flow Through Branch 204 16.3.3 Converging Flow into Branch 207 16.4 Full-Flow Through Run 208 References 226 Further Reading 226 17 Pipe Joints 229 17.1 Weld Protrusion 229 17.2 Backing Rings 230 17.3 Misalignment 231 17.3.1 Misaligned Pipe 231 17.3.2 Misaligned Gasket 231 18 Valves 233 18.1 Multiturn Valves 233 18.1.1 Diaphragm Valve 233 18.1.2 Gate Valve 234 18.1.3 Globe Valve 234 18.1.4 Pinch Valve 235 18.1.5 Needle Valve 235 18.2 Quarter-Turn Valves 236 18.2.1 Ball Valve 236 18.2.2 Butterfly Valve 236 18.2.3 Plug Valve 236 18.3 Self-Actuated Valves 237 18.3.1 Check Valve 237 18.3.2 Relief Valve 238 18.4 Control Valves 239 18.5 Valve Loss Coefficients 239 References 240 Further Reading 240 19 Threaded Fittings 241 19.1 Reducers: Contracting 241 19.2 Reducers: Expanding 241 19.3 Elbows 242 19.4 Tees 242 19.5 Couplings 242 19.6 Valves 243 Reference 243 Further Reading 243 Part III Flow Phenomena 245 20 Cavitation 247 20.1 The Nature of Cavitation 247 20.2 Pipeline Design 248 20.3 Net Positive Suction Head 248 20.4 Example Problem: Core Spray Pump NPSH 249 20.4.1 New, Clean Steel Pipe 250 20.4.1.1 Input Parameters 250 20.4.1.2 Solution 250 20.4.1.3 Results 250 20.4.2 Moderately Corroded Steel Pipe 251 20.4.2.1 Input Parameters 251 20.4.2.2 Solution 251 20.4.2.3 Results 251 20.5 Example Problem: Pipe Entrance Cavitation 252 20.5.1 Input Parameters 252 20.5.2 Calculations and Results 253 Reference 253 Further Reading 254 21 Flow-induced Vibration 255 21.1 Steady Internal Flow 255 21.2 Steady External Flow 255 21.3 Water Hammer 256 21.4 Column Separation 258 References 258 Further Reading 258 22 Temperature Rise 261 22.1 Head Loss 261 22.2 Pump Temperature Rise 261 22.3 Example Problem: Reactor Heat Balance 262 22.4 Example Problem: Vessel Heat-Up 262 22.5 Example Problem: Pumping System Temperature 262 References 263 23 Flow to Run Full 265 23.1 Open Flow 265 23.2 Full Flow 266 23.3 Submerged Flow 268 23.4 Example Problem: Reactor Application 269 Further Reading 270 24 Jet Pump Performance 271 24.1 Performance Characteristics 271 24.2 Mixing Section Model 272 24.2.1 Momentum Balance 273 24.2.2 Drive Flow Mixing Coefficient 273 24.2.3 Suction Flow Mixing Coefficient 273 24.2.4 Discharge Flow Density 274 24.2.5 Discharge Flow Viscosity 274 24.3 Component Flow Losses 274 24.3.1 Surface Friction 274 24.3.2 Loss Coefficients 274 24.4 Hydraulic Performance Flow Paths 276 24.4.1 Drive Flow Path 276 24.4.2 Suction Flow Path 276 24.5 Flow Model Validation 276 24.6 Example Problem: Water-Water Jet Pump 278 24.6.1 Flow Conditions 278 24.6.2 Jet Pump Geometry 278 24.6.3 Preliminary Calculations 278 24.6.4 Loss Coefficients 279 24.6.5 Predicted Performance 280 24.7 Parametric Studies 281 24.7.1 Surface Finish Differences 281 24.7.2 Nozzle to Throat Area Ratio Variation 282 24.7.3 Density Differences 282 24.7.4 Viscosity Differences 282 24.7.5 Straight Line and Parabolic Performance Representations 283 24.8 Epilogue 283 References 283 Further Reading 283 Appendix A Physical Properties of Water at 1 Atmosphere 287 Appendix B Pipe Size Data 291 Appendix C Physical Constants and Unit Conversions 299 Appendix D Compressibility Factor Equations 311 D.1 The Redlich-Kwong Equation 311 D.2 The Lee-Kesler Equation 312 D.3 Important Constants for Selected Gases 314 D.4 Compressibility Chart 314 Appendix E Adiabatic Compressible Flow with Friction Using Mach Number as a Parameter 319 E.1 Solution when Static Pressure and Static Temperature are Known 319 E.2 Solution when Static Pressure and Total Temperature are Known 322 E.3 Solution when Total Pressure and Total Temperature are Known 322 E.4 Solution when Total Pressure and Static Temperature are Known 324 References 325 Appendix F Velocity Profile Equations 327 F.1 Benedict Velocity Profile Derivation 327 F.2 Street, Watters, and Vennard Velocity Profile Derivation 329 References 330 Appendix G Speed of Sound in Water 331 Appendix H Jet Pump Performance Program 333 Index 343