Near-boundary Fluid Mechanics /
Near-Boundary Fluid Mechanics focuses on the near-boundary region and its significance.It delves into topics like boundary shear stress, drag reduction using polymer additives, turbulence sources, secondary currents, log-law validity, sediment transport, and more.Unlike similar books, it emphasizes...
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| Corporate Author: | |
| Format: | eBook |
| Language: | English |
| Published: |
London ; San Diego, CA :
Academic Press, an imprint of Elsevier,
[2025]
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| Series: | Multiphysics. advances and applications.
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| Subjects: | |
| Online Access: | Connect to the full text of this electronic book |
Table of Contents:
- Front Cover
- Near-Boundary Fluid Mechanics
- Copyright Page
- Contents
- About the author
- Foreword
- Preface
- 1 Is flow region divisible responding to its boundary?
- 2 Reynolds time-average method or event-based average method?
- 3 Energy method or force method
- 4 Problems to be discussed
- 4.1 Circular pipe (2D) flow
- 4.2 Noncircular (3D) pipe flow
- 4.3 Loose boundary flows
- 4.4 External flows
- 4.5 Drag reduction flows
- 4.6 Coherent structures
- 1 Introduction to governing equations
- 1.1 Classification of fluid flows
- 1.2 Units and dimensional analysis
- 1.3 Historical progress in fluid mechanics
- 1.3.1 Archimedes' principle-interpretation and extension
- 1.3.2 Isaac Newton's fluid friction-interpretation and extension
- 1.3.3 Daniel Bernoulli and his principle-energy approach
- 1.3.4 Leonhard Euler and the governing equations of ideal fluids
- 1.3.5 Navier-Stokes equations for real fluid flows
- 1.4 Progress toward solution of N-S equations
- 1.4.1 Reynolds and his time-average approach (1895)
- 1.4.2 Prandtl and boundary layer theory (1904)
- 1.4.3 Kolmogorov and statistical theory
- 1.4.4 Fick's diffusion and Taylor's method
- 1.4.5 Nikora's double-averaging concept
- 1.5 Airy wave theory (inviscid fluid)
- 1.5.1 Governing equations and boundary conditions
- 1.5.2 Solution of Airy wave
- 1.5.3 Wave energy
- 1.5.4 Nonlinear wave theory
- 1.5.5 Tidal waves
- 1.6 Conclusions
- Nomenclature
- References
- Further reading
- 2 One-dimensional internal flow
- 2.1 Uniform and gradually varied open channel flows (a≈0)
- 2.1.1 Basic concepts
- 2.1.2 Uniform flow (a=0)
- 2.1.3 Interpretation of hydraulic radius and best cross-section
- 2.1.4 Equation of gradually varied flow (a≈0)
- 2.1.5 Water surface profiles in gradually varied flow
- 2.2 Rapid varied open-channel flows (a≠0).
- 2.2.1 Specific energy
- 2.2.2 Channel transition
- 2.2.3 Hydraulic jump
- 2.2.4 Energy losses in accelerating/decelerating flows
- 2.3 Pipe flows
- 2.3.1 Pipe network and friction loss (a=0)
- 2.3.2 Energy loss in contraction (a>
- 0) and expansion (a<
- 0)
- 2.3.3 Minor loss (a<
- 0)
- 2.4 Flow measurement (a>
- 0)
- 2.4.1 Weirs in open channels
- 2.4.2 Pipe flows
- 2.5 Eddy inertial force
- 2.5.1 Eddy volume and eddy inertial force
- 2.5.2 Venturi flume and loss coefficient KL
- 2.5.3 Work, energy, power, and eddy force
- 2.5.4 Superposition of skin friction and eddy drag
- 2.6 Conclusions
- Nomenclature
- References
- 3 Internal, steady, and uniform two-dimensional flows (a=0)
- 3.1 Flows in pipes and open channels
- 3.1.1 Laminar flows and N-S equations
- 3.1.2 Turbulent flows and Reynolds equations
- 3.1.3 Reynolds shear stress and log-law in smooth channels
- 3.1.4 Effect of roughened boundary
- 3.2 Dou Guo-Ren's stochastic theory
- 3.2.1 Stochastic theory
- 3.2.2 Mechanism of flow passing over roughness elements
- 3.2.3 Probability of turbulence occurrence
- 3.2.4 Turbulent structures
- 3.3 Applications of Dou's theory
- 3.3.1 Velocity distribution in smooth channels
- 3.3.2 Turbulent structures
- 3.3.3 General laws for friction factor
- 3.4 Viscoelastic flow of polymer solution
- 3.4.1 Non-Newtonian fluid and its stress/strain relationship
- 3.4.2 Velocity and turbulent intensity profiles
- 3.4.3 Drag reduction (Dr) parameter
- 3.4.4 Drag coefficient
- 3.5 Progress in turbulence research
- 3.5.1 Reynolds shear stress and velocity distribution (v≠0)
- 3.5.2 Velocity u+ distributions
- 3.5.3 Turbulent intensity and energy spectrum
- 3.5.4 Roughness mechanism
- 3.5.5 Friction factor
- 3.6 Progress in drag reduction flow research
- 3.6.1 Universal drag reduction mechanism.
- 3.6.2 Onset conditions and optimum concentration
- 3.6.3 Velocity distribution and friction factor
- 3.6.4 Roughness effect and laminar-turbulent transition
- 3.6.5 Energy spectrum and turbulent structures
- 3.6.5.1 Turbulent structures
- 3.6.5.2 Energy spectrum
- 3.7 Separation flow of large roughness element
- 3.7.1 Theoretical investigation
- 3.7.2 Comparison with experimental data
- 3.7.3 Interpretation and applications
- 3.8 Conclusions
- Nomenclature
- References
- Further reading
- 4 Steady and nonuniform flows or unsteady flows (a≠0)
- 4.1 Introduction
- 4.2 Unsteady 1D flow (∂/∂t≠0)
- 4.2.1 Saint-Venant equations for open channels
- 4.2.2 Other methods for unsteady open channel flows
- 4.2.3 Surges in open channels
- 4.2.4 Water hammer in pipes
- 4.2.5 Mass flux
- 4.3 Steady accelerating 2D flows (∂/∂t=0, ∂u/∂x>
- 0)
- 4.3.1 Theoretical investigations
- 4.3.2 Total shear stress distribution
- 4.3.3 Mechanism of dip-phenomenon
- 4.4 Steady decelerating 2D flows (∂/∂t=0, ∂u/∂x<
- 0)
- 4.4.1 Mechanism of wake law
- 4.4.2 Turbulent structures
- 4.4.3 Others' research
- 4.5 Unsteady 2D flows (∂/∂t≠0)
- 4.5.1 Governing equations
- 4.5.2 Velocity profiles
- 4.5.3 Turbulent structures
- 4.5.4 Acceleration and velocity deviation from the log-law
- 4.5.5 Friction factor and pipe flow
- 4.6 Conclusions
- Nomenclature
- References
- 5 Mechanism of energy transport and boundary shear stress distribution in 3D flows
- 5.1 Introduction
- 5.1.1 Energy and force approaches
- 5.1.2 Principle of least time for a ray path
- 5.1.3 Yield lines in plates
- 5.1.4 Hydraulic radius and boundary shear stress
- 5.2 Mechanism of energy transport
- 5.2.1 Two-dimensional flows
- 5.2.2 Three Dimensional flows
- 5.2.3 Yang's principle of "surplus energy transport toward the nearest boundary".
- 6.3.3 Rectangular duct flows
- 6.3.4 Mechanism of dip-phenomenon
- 6.3.5 Velocity in rectangular open channel flows
- 6.3.6 Other channel flows
- 6.4 Velocity profiles in roughened channels
- 6.4.1 Uniform roughness distribution along wetted perimeter
- 6.4.2 Nonuniform roughness distribution along wetted perimeter
- 6.4.3 Coexistence of rough and smooth boundaries
- 6.4.4 Diffusion coefficient and dispersion
- 6.5 Friction factors
- 6.5.1 Pipes of noncircular cross-section
- 6.5.2 Sidewall correction
- 6.5.2.1 Einstein, H. A
- 6.5.2.2 Jiang (1948)
- 6.5.2.3 Chow's (1973) method
- 6.5.2.4 Guo-ren Dou's (1978) method
- 6.5.2.5 Nian-Sheng Cheng's (2005) method
- 6.5.3 Theoretical extension from 2D flow to 3D flows
- 6.5.4 Smooth channels
- 6.5.5 Composite roughness on boundaries
- 6.6 Conclusions
- Nomenclature
- References
- 7 Time-averaged and event-averaged Navier-Stokes equations
- 7.1 Introduction
- 7.2 Revisit Reynolds' (1883) experiment and his (1895) interpretations
- 7.2.1 Reynolds' original idea and comparison with other great ideas
- 7.2.2 Reynolds number and time-average method
- 7.2.3 Limitations of the time-averaged method
- 7.3 Advances in experimental and theoretical research
- 7.3.1 The bursting phenomenon and coherent structures
- 7.3.2 Princeton's super velocity and log-law's validity
- 7.3.3 Quadrant analysis
- 7.3.4 Log-law or power law?
- 7.4 Event-based averaged Navier-Stokes equation
- 7.4.1 Why Navier-Stokes equations should be event-averaged
- 7.4.2 How to average Navier-Stokes equations based on events
- 7.4.3 Turbulence, waves on interface caused by bursting/kolk-boiler phenomenon
- 7.4.4 Intermittency and energy losses
- 7.4.5 Why log-law is invalid at high Reynolds number
- 7.5 Comparisons and predictions in cases of v>
- 0, v<
- 0, and v=0.