CITATION

Potter, Merle and Wiggert, David. Schaum's Outline of Fluid Mechanics. US: McGraw-Hill, 2007.

Schaum's Outline of Fluid Mechanics

Published:  December 2007

eISBN: 9780071594547 007159454X | ISBN: 9780071487818
  • Contents
  • Chapter 1 Basic Information
  • 1.1 Introduction
  • 1.2 Dimensions, Units, and Physical Quantities
  • 1.3 Gases and Liquids
  • 1.4 Pressure and Temperature
  • 1.5 Properties of Fluids
  • 1.6 Thermodynamic Properties and Relationships
  • Chapter 2 Fluid Statics
  • 2.1 Introduction
  • 2.2 Pressure Variation
  • 2.3 Manometers
  • 2.4 Forces on Plane and Curved Surfaces
  • 2.5 Accelerating Containers
  • Chapter 3 Fluids in Motion
  • 3.1 Introduction
  • 3.2 Fluid Motion
  • 3.2.1 Lagrangian and Eulerian Descriptions
  • 3.2.2 Pathlines, Streaklines, and Streamlines
  • 3.2.3 Acceleration
  • 3.2.4 Angular Velocity and Vorticity
  • 3.3 Classification of Fluid Flows
  • 3.3.1 Uniform, One-, Two-, and Three-Dimensional Flows
  • 3.3.2 Viscous and Inviscid Flows
  • 3.3.3 Laminar and Turbulent Flows
  • 3.3.4 Incompressible and Compressible Flows
  • 3.4 Bernoulli’s Equation
  • Chapter 4 The Integral Equations
  • 4.1 Introduction
  • 4.2 System-to-Control-Volume Transformation
  • 4.3 Conservation of Mass
  • 4.4 The Energy Equation
  • 4.5 The Momentum Equation
  • Chapter 5 Differential Equations
  • 5.1 Introduction
  • 5.2 The Differential Continuity Equation
  • 5.3 The Differential Momentum Equation
  • 5.4 The Differential Energy Equation
  • Chapter 6 Dimensional Analysis and Similitude
  • 6.1 Introduction
  • 6.2 Dimensional Analysis
  • 6.3 Similitude
  • Chapter 7 Internal Flows
  • 7.1 Introduction
  • 7.2 Entrance Flow
  • 7.3 Laminar Flow in a Pipe
  • 7.3.1 The Elemental Approach
  • 7.3.2 Applying the Navier–Stokes Equations
  • 7.3.3 Quantities of Interest
  • 7.4 Laminar Flow Between Parallel Plates
  • 7.4.1 The Elemental Approach
  • 7.4.2 Applying the Navier–Stokes Equations
  • 7.4.3 Quantities of Interest
  • 7.5 Laminar Flow between Rotating Cylinders
  • 7.5.1 The Elemental Approach
  • 7.5.2 Applying the Navier–Stokes Equations
  • 7.5.3 Quantities of Interest
  • 7.6 Turbulent Flow in a Pipe
  • 7.6.1 The Semi-Log Profile
  • 7.6.2 The Power-Law Profile
  • 7.6.3 Losses in Pipe Flow
  • 7.6.4 Losses in Noncircular Conduits
  • 7.6.5 Minor Losses
  • 7.6.6 Hydraulic and Energy Grade Lines
  • 7.7 Open Channel Flow
  • Chapter 8 External Flows
  • 8.1 Introduction
  • 8.2 Flow Around Blunt Bodies
  • 8.2.1 Drag Coefficients
  • 8.2.2 Vortex Shedding
  • 8.2.3 Cavitation
  • 8.2.4 Added Mass
  • 8.3 Flow Around Airfoils
  • 8.4 Potential Flow
  • 8.4.1 Basics
  • 8.4.2 Several Simple Flows
  • 8.4.3 Superimposed Flows
  • 8.5 Boundary-Layer Flow
  • 8.5.1 General Information
  • 8.5.2 The Integral Equations
  • 8.5.3 Laminar and Turbulent Boundary Layers
  • 8.5.4 Laminar Boundary-Layer Differential Equations
  • Chapter 9 Compressible Flow
  • 9.1 Introduction
  • 9.2 Speed of Sound
  • 9.3 Isentropic Nozzle Flow
  • 9.4 Normal Shock Waves
  • 9.5 Oblique Shock Waves
  • 9.6 Expansion Waves
  • Chapter 10 Flow in Pipes and Pumps
  • 10.1 Introduction
  • 10.2 Simple Pipe Systems
  • 10.2.1 Losses
  • 10.2.2 Hydraulics of Simple Pipe Systems
  • 10.3 Pumps in Pipe Systems
  • 10.4 Pipe Networks
  • 10.4.1 Network Equations
  • 10.4.2 Hardy Cross Method
  • 10.4.3 Computer Analysis of Network Systems
  • 10.5 Unsteady Flow
  • 10.5.1 Incompressible Flow
  • 10.5.2 Compressible Flow of Liquids
  • Appendix A: Units and Conversions
  • A.1 English Units, SI Units, and Their Conversion Factors
  • A.2 Conversions of Units
  • Appendix B: Vector Relationships
  • Appendix C: Fluid Properties
  • C.1 Properties of Water
  • C.1E: English Properties of Water
  • C.2 Properties of Air at Atmospheric Pressure
  • C.2E: English Properties of Air at Atmospheric Pressure
  • C.3 Properties of the Standard Atmosphere
  • C.3E: English Properties of the Atmosphere
  • C.4 Properties of Ideal Gases at 300 K (c[sub(v)] = c[sub(p)] – k k = c[sub(p)]/c[sub(v)])
  • C.5 Properties of Common Liquids at Atmospheric Pressure and Approximately 16 to 21°C (60 to 70°F)
  • Figure C.1 Viscosity as a Function of Temperature
  • Figure C.2 Kinematic Viscosity as a Function of Temperature at Atmospheric Pressure
  • Appendix D: Compressible Flow Table for Air
  • D.1 Isentropic Flow
  • D.2 Normal Shock Flow
  • D.3 Prandtl–Meyer Function
  • Index