Cambridge University Press
978-0-521-84910-4 - Advanced Transport Phenomena - Fluid Mechanics and Convective Transport Processes - by L. Gary Leal
Frontmatter/Prelims



ADVANCED TRANSPORT PHENOMENA



Advanced Transport Phenomena is ideal as a graduate textbook. It contains a detailed discussion of modern analytic methods for the solution of fluid mechanics and heat and mass transfer problems, focusing on approximations based on scaling and asymptotic methods, beginning with the derivation of basic equations and boundary conditions and concluding with linear stability theory. Also covered are unidirectional flows, lubrication and thin-film theory, creeping flows, boundary-layer theory, and convective heat and mass transport at high and low Reynolds numbers. The emphasis is on basic physics, scaling and nondimensionalization, and approximations that can be used to obtain solutions that are due either to geometric simplifications, or large or small values of dimensionless parameters. The author emphasizes setting up problems and extracting as much information as possible short of obtaining detailed solutions of differential equations. The book also focuses on the solutions of representative problems. This reflects the author’s bias toward learning to think about the solution of transport problems.

L. Gary Leal is professor of chemical engineering at the University of California in Santa Barbara. He also holds positions in the Materials Department and in the Department of Mechanical Engineering. He has taught at UCSB since 1989. Before that, from 1970 to 1989 he taught in the chemical engineering department at Caltech. His current research interests are focused on fluid mechanics problems for complex fluids, as well as the dynamics of bubbles and drops in flow, coalescence, thin-film stability, and related problems in rheology. In 1987, he was elected to the National Academy of Engineering. His research and teaching have been recognized by a number of awards, including the Dreyfus Foundation Teacher-Scholar Award, a Guggenheim Fellowship, the Allan Colburn and Warren Walker Awards of the AIChE, the Bingham Medal of the Society of Rheology, and the Fluid Dynamics Prize of the American Physical Society. Since 1995, Professor Leal has been one of the two editors of the AIP journal Physics of Fluids and he has also served on the editorial boards of numerous journals and the Cambridge Series in Chemical Engineering.





CAMBRIDGE SERIES IN CHEMICAL ENGINEERING



Series Editor:

Arvind Varma, Purdue University


Editorial Board:

Alexis T. Bell, University of California, Berkeley
Edward Cussler, University of Minnesota
Mark E. Davis, California Institute of Technology
L. Gary Leal, University of California, Santa Barbara
Massimo Morbidelli, ETH, Zurich
Athanassios Z. Panagiotopoulos, Princeton University
Stanley I. Sandler, University of Delaware
Michael L. Schuler, Cornell University


Books in the Series:

E. L. Cussler, Diffusion: Mass Transfer in Fluid Systems, Second Edition

Liang-Shih Fan and Chao Zhu, Principles of Gas-Solid Flows

Hasan Orbey and Stanley I. Sandler, Modeling Vapor-Liquid Equilibria: Cubic Equations of State and Their Mixing Rules

T. Michael Duncan and Jeffrey A. Reimer, Chemical Engineering Design and Analysis: An Introduction

John C. Slattery, Advanced Transport Phenomena

A. Varma, M. Morbidelli, and H. Wu, Parametric Sensitivity in Chemical Systems

M. Morbidelli, A. Gavriilidis, and A. Varma, Catalyst Design: Optimal Distribution of Catalyst in Pellets, Reactors, and Membranes

E. L. Cussler and G. D. Moggridge, Chemical Product Design

Pao C. Chau, Process Control: A First Course with MATLAB®

Richard Noble and Patricia Terry, Principles of Chemical Separations with Environmental Applications

F. B. Petlyuk, Distillation Theory and Its Application to Optimal Design of Separation Units

Leal, L. Gary, Advanced Transport Phenomena: Fluid Mechanics and Convective Transport





Advanced Transport Phenomena



Fluid Mechanics and Convective Transport Processes



L. Gary Leal





CAMBRIDGE UNIVERSITY PRESS
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First published 2007

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Library of Congress Cataloging in Publication Data

Leal, L. Gary.
Advanced transport phenomena : fluid mechanics and convective trasport processes / L. Gary Leal.
   p. cm. – (Cambridge series in chemical engineering)
Includes bibliographical references and index.
ISBN-13: 978-0-521-84910-4 (hardback)
ISBN-10: 0-521-84910-1 (hardback)
1. Fluid mechanics – Textbooks. 2. Transport theory – Textbooks. 3. Continuum mechanics –
Textbooks. I. Title. II. Series.
QC145.2.L43  2007
660′.2842 – dc22      2006018348

ISBN 978-0-521-84910-4 hardback

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third-party Internet Web sites referred to in this publication
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Contents



Preface page xv
Acknowledgments xix
1   A Preview 1
  A   A Brief Historical Perspective of Transport Phenomena in Chemical Engineering 1
  B   The Nature of the Subject 2
  C   A Brief Description of the Contents of This Book 4
  Notes and References 11
2   Basic Principles 13
  A   The Continuum Approximation 13
      1  Foundations 14
      2  Consequences 15
  B   Conservation of Mass – The Continuity Equation 18
  C   Newton’s Laws of Mechanics 25
  D   Conservation of Energy and the Entropy Inequality 31
  E   Constitutive Equations 36
  F   Fluid Statics – The Stress Tensor for a Stationary Fluid 37
  G   The Constitutive Equation for the Heat Flux Vector – Fourier’s Law 42
  H   Constitutive Equations for a Flowing Fluid – The Newtonian Fluid 45
  I   The Equations of Motion for a Newtonian Fluid – The Navier–Stokes Equation 49
  J   Complex Fluids – Origins of Non-Newtonian Behavior 52
  K   Constitutive Equations for Non-Newtonian Fluids 59
  L   Boundary Conditions at Solid Walls and Fluid Interfaces 65
      1  The Kinematic Condition 67
      2  Thermal Boundary Conditions 68
      3  The Dynamic Boundary Condition 69
  M   Further Considerations of the Boundary Conditions at the Interface Between Two Pure Fluids – The Stress Conditions 74
      3  Generalization of the Kinematic Boundary Condition for an Interface 75
      2  The Stress Conditions 76
      3  The Normal-Stress Balance and Capillary Flows 79
      4  The Tangential-Stress Balance and Thermocapillary Flows 84
  N   The Role of Surfactants in the Boundary Conditions at a Fluid Interface 89
  Notes and Reference 96
  Problems 99
3   Unidirectional and One-Dimensional Flow and Heat Transfer Problems 110
  A   Simplification of the Navier–Stokes Equations for Unidirectional Flows 113
  B   Steady Unidirectional Flows – Nondimensionalization and Characteristic Scales 115
  C   Circular Couette Flow – A One-Dimensional Analog to Unidirectional Flows 125
  D   Start-Up Flow in a Circular Tube – Solution by Separation of Variables 135
  E   The Rayleigh Problem – Solution by Similarity Transformation 142
  F   Start-Up of Simple Shear Flow 148
  G   Solidification at a Planar Interface 152
  H   Heat Transfer in Unidirectional Flows 157
      1  Steady-State Heat Transfer in Fully Developed Flow through a Heated (or Cooled) Section of a Circular Tube 158
      2  Taylor Diffusion in a Circular Tube 166
  I   Pulsatile Flow in a Circular Tube 175
  Notes 183
  Problems 185
4   An Introduction to Asymptotic Approximations 204
  A   Pulsatile Flow in a Circular Tube Revisited – Asymptotic Solutions for High and Low Frequencies 205
      1  Asymptotic Solution for Rω1 206
      2  Asymptotic Solution for Rω1 209
  B   Asymptotic Expansions – General Considerations 216
  C   The Effect of Viscous Dissipation on a Simple Shear Flow 219
  D   The Motion of a Fluid Through a Slightly Curved Tube – The Dean Problem 224
  E   Flow in a Wavy-Wall Channel – “Domain Perturbation Method” 232
      1  Flow Parallel to the Corrugation Grooves 233
      2  Flow Perpendicular to the Corrugation Grooves 237
  F   Diffusion in a Sphere with Fast Reaction – “Singular Perturbation Theory” 242
  G   Bubble Dynamics in a Quiescent Fluid 250
      1  The Rayleigh–Plesset Equation 251
      2  Equilibrium Solutions and Their Stability 255
      3  Bubble Oscillations Due to Periodic Pressure Oscillations – Resonance and “Multiple-Time-Scale Analysis” 260
      4  Stability to Nonspherical Disturbances 269
  Notes 282
  Problems 284
5   The Thin-Gap Approximation – Lubrication Problems 294
  A   The Eccentric Cylinder Problem 295
      1  The Narrow-Gap Limit – Governing Equations and Solutions 297
      2  Lubrication Forces 303
  B   Derivation of the Basic Equations of Lubrication Theory 306
  C   Applications of Lubrication Theory 315
      1  The Slider-Block Problem 315
      2  The Motion of a Sphere Toward a Solid, Plane Boundary 320
  D   The Air Hockey Table 325
      1  The Lubrication Limit, R̃e1 328
      2  The Uniform Blowing Limit, p*R1 332
        a  R̃e1 334
        b  R̃e1 336
        c  Lift on the Disk 345
  Notes 346
  Problems 347
6   The Thin-Gap Approximation – Films with a Free Surface 355
  A   Derivation of the Governing Equations 355
      1  The Basic Equations and Boundary Conditions 355
      2  Simplification of the Interface Boundary Conditions for a Thin Film 359
      3  Derivation of the Dynamical Equation for the Shape Function, h(Xs, t) 360
  B   Self-Similar Solutions of Nonlinear Diffusion Equations 362
  C   Films with a Free Surface – Spreading Films on a Horizontal Surface 367
      1  Gravitational Spreading 367
      2  Capillary Spreading 371
  D   The Dynamics of a Thin Film in the Presence of van der Waals Forces 376
      1  Linear Stability 378
      2  Similarity Solutions for Film Rupture 381
  E   Shallow-Cavity Flows 385
      1  The Horizontal, Enclosed Shallow Cavity 386
      2  The Horizontal Shallow Cavity with a Free Surface 391
        a  Solution by means of the classical thin-film analysis 392
        b  Solution by means of the method of domain perturbations 396
        c  The end regions 401
      3  Thermocapillary Flow in a Thin Cavity 404
        a  Thin-film solution procedure 410
        b  Solution by domain perturbation for δ = 1 413
  Notes 418
  Problems 418
7   Creeping Flow – Two-Dimensional and Axisymmetric Problems 429
  A   Nondimensionalization and the Creeping-Flow Equations 430
  B   Some General Consequences of Linearity and the Creeping-Flow Equations 434
      1  The Drag on Bodies That Are Mirror Images in the Direction of Motion 434
      2  The Lift on a Sphere That is Rotating in a Simple Shear Flow 436
      3  Lateral Migration of a Sphere in Poiseuille Flow 438
      4  Resistance Matrices for the Force and Torque on a Body in Creeping Flow 439
  C   Representation of Two-Dimensional and Axisymmetric Flows in Terms of the Streamfunction 444
  D   Two-Dimensional Creeping Flows: Solutions by Means of Eigenfunction Expansions (Separation of Variables) 449
      1  General Eigenfunction Expansions in Cartesian and Cylindrical Coordinates 449
      2  Application to Two-Dimensional Flow near Corners 451
  E   Axisymmetric Creeping Flows: Solution by Means of Eigenfunction Expansions in Spherical Coordinates (Separation of Variables) 458
      1  General Eigenfunction Expansion 459
      2  Application to Uniform Streaming Flow past an Arbitrary Axisymmetric Body 464
  F   Uniform Streaming Flow past a Solid Sphere – Stokes’ Law 466
  G   A Rigid Sphere in Axisymmetric, Extensional Flow 470
      1  The Flow Field 470
      2  Dilute Suspension Rheology – The Einstein Viscosity Formula 473
  H   Translation of a Drop Through a Quiescent Fluid at Low Re 477
  I   Marangoni Effects on the Motion of Bubbles and Drops 486
  J   Surfactant Effects on the Buoyancy-Driven Motion of a Drop 490
      1  Governing Equations and Boundary Conditions for a Translating Drop with Surfactant Adsorbed at the Interface 493
      2  The Spherical-Cap Limit 497
      3  The Limit of Fast Adsorption Kinetics 503
  Notes 510
  Problems 512
8   Creeping Flow – Three-Dimensional Problems 524
  A   Solutions by Means of Superposition of Vector Harmonic Functions 525
      1  Preliminary Concepts 525
        a  Vector “equality” – pseudo-vectors 525
        b  Representation theorem for solution of the creeping-flow equations 526
        c  Vector harmonic functions 527
      2  The Rotating Sphere in a Quiescent Fluid 528
      3  Uniform Flow past a Sphere 529
  B   A Sphere in a General Linear Flow 530
  C   Deformation of a Drop in a General Linear Flow 537
  D   Fundamental Solutions of the Creeping-Flow Equations 545
      1  The “Stokeslet”: A Fundamental Solution for the Creeping-Flow Equations 545
      2  An Integral Representation for Solutions of the Creeping-Flow Equations due to Ladyzhenskaya 547
  E   Solutions for Solid Bodies by Means of Internal Distributions of Singularities 550
      1  Fundamental Solutions for a Force Dipole and Other Higher-Order Singularities 551
      2  Translation of a Sphere in a Quiescent Fluid (Stokes’ Solution) 554
      3  Sphere in Linear Flows: Axisymmetric Extensional Flow and Simple Shear 555
      4  Uniform Flow past a Prolate Spheroid 557
      5  Approximate Solutions of the Creeping-Flow Equations by Means of Slender-Body Theory 560
  F   The Boundary Integral Method 564
      1  A Rigid Body in an Unbounded Domain 565
      2  Problems Involving a Fluid Interface 565
      3  Problems in a Bounded Domain 568
  G   Further Topics in Creeping-Flow Theory 570
      1  The Reciprocal Theorem 571
      2  Faxen’s Law for a Body in an Unbounded Fluid 571
      3  Inertial and Non-Newtonian Corrections to the Force on a Body 573
      4  Hydrodynamic Interactions Between Widely Separated Particles – The Method of Reflections 576
  Notes 580
  Problems 582
9   Convection Effects in Low-Reynolds-Number Flows 593
  A   Forced Convection Heat Transfer – Introduction 593
      1  General Considerations 594
      2  Scaling and the Dimensionless Parameters for Convective Heat Transfer 596
      3  The Analogy with Single-Solute Mass Transfer 598
  B   Heat Transfer by Conduction (Pe → 0) 600
  C   Heat Transfer from a Solid Sphere in a Uniform Streaming Flow at Small, but Nonzero, Peclet Numbers 602
      1  Introduction – Whitehead’s Paradox 602
      2  Expansion in the Inner Region 605
      3  Expansion in the Outer Region 606
      4  A Second Approximation in the Inner Region 611
      5  Higher-Order Approximations 613
      6  Specified Heat Flux 615
  D   Uniform Flow past a Solid Sphere at Small, but Nonzero, Reynolds Number 616
  E   Heat Transfer from a Body of Arbitrary Shape in a Uniform Streaming Flow at Small, but Nonzero, Peclet Numbers 627
  F   Heat Transfer from a Sphere in Simple Shear Flow at Low Peclet Numbers 633
  G   Strong Convection Effects in Heat and Mass Transfer at Low Reynolds Number – An Introduction 643
  H   Heat Transfer from a Solid Sphere in Uniform Flow for Re1 and Pe1 645
      1  Governing Equations and Rescaling in the Thermal Boundary-Layer Region 648
      2  Solution of the Thermal Boundary-Layer Equation 652
  I   Thermal Boundary-Layer Theory for Solid Bodies of Nonspherical Shape in Uniform Streaming Flow 656
      1  Two-Dimensional Bodies 659
      2  Axisymmetric Bodies 661
      3  Problems with Closed Streamlines (or Stream Surfaces) 662
  J   Boundary-Layer Analysis of Heat Transfer from a Solid Sphere in Generalized Shear Flows at Low Reynolds Number 663
  K   Heat (or Mass) Transfer Across a Fluid Interface for Large Peclet Numbers 666
      1  General Principles 666
      2  Mass Transfer from a Rising Bubble or Drop in a Quiescent Fluid 668
  L   Heat Transfer at High Peclet Number Across Regions of Closed-Streamline Flow 671
      1  General Principles 671
      2  Heat Transfer from a Rotating Cylinder in Simple Shear Flow 672
  Notes 680
  Problems 681
10   Laminar Boundary-Layer Theory 697
  A   Potential-Flow Theory 698
  B   The Boundary-Layer Equations 704
  C   Streaming Flow past a Horizontal Flat Plate – The Blasius Solution 713
  D   Streaming Flow past a Semi-Infinite Wedge – The Falkner–Skan Solutions 719
  E   Streaming Flow past Cylindrical Bodies – Boundary-Layer Separation 725
  F   Streaming Flow past Axisymmetric Bodies – A Generalizaiton of the Blasius Series 733
  G   The Boundary-Layer on a Spherical Bubble 739
  Notes 754
  Problems 756
11   Heat and Mass Transfer at Large Reynolds Number 767
  A   Governing Equations (Re1, Pe1, with Arbitrary Pr or Sc numbers) 769
  B   Exact (Similarity) Solutions for Pr (or Sc) ∼ O(1) 771
  C   The Asymptotic Limit, Pr(or Sc) ≫ 1 773
  D   The Asymptotic Limit, Pr(or Sc) ≪ 1 780
  E   Use of the Asymptotic Results at Intermediate Pe(or Sc) 787
  F   Approximate Results for Surface Temperature with Specified Heat Flux or Mixed Boundary Conditions 788
  G   Laminar Boundary-Layer Mass Transfer for Finite Interfacial Velocities 793
  Notes 797
  Problems 797
12   Hydrodynamic Stability 800
  A   Capillary Instability of a Liquid Thread 801
      1  The Inviscid Limit 804
      2  Viscous Effects on Capillary Instability 808
      3  Final Remarks 811
  B   Rayleigh–Taylor Instability (The Stability of a Pair of Immiscible Fluids That Are Separated by a Horizontal Interface) 812
      1  The Inviscid Fluid Limit 816
      2  The Effects of Viscosity on the Stability of a Pair of Superposed Fluids 818
      3  Discussion 822
  C   Saffman–Taylor Instability at a Liquid Interface 823
      1  Darcy’s Law 823
      2  The Taylor–Saffman Instability Criteria 826
  D   Taylor–Couette Instability 829
      1  A Sufficient Condition for Stability of an Inviscid Fluid 832
      2  Viscous Effects 835
  E   Nonisothermal and Compositionally Nonuniform Systems 840
  F   Natural Convection in a Horizontal Fluid Layer Heated from Below – The Rayleigh–Benard Problem 845
      1  The Disturbance Equations and Boundary Conditions 845
      2  Stability for Two Free Surfaces 851
      3  The Principle of Exchange of Stabilities 853
      4  Stability for Two No-Slip, Rigid Boundaries 855
  G   Double-Diffusive Convection 858
  H   Marangoni Instability 867
  I   Instability of Two-Dimensional Unidirectional Shear Flows 872
      1  Inviscid Fluids 873
        a  The Rayleigh stability equation 873
        b  The Inflection-point theorem 875
      2  Viscous Fluids 876
        a  The Orr–Sommerfeld equation 876
        b  A sufficient condition for stability 877
  Notes 878
  Problems 880
Appendix A: Governing Equations and Vector Operations in Cartesian, Cylindrical, and Spherical Coordinate Systems 891
Appendix B: Cartesian Component Notation 897
Index 899




Preface



This book represents a major revision of my book Laminar Flow and Convective Transport Processes that was published in 1992 by Butterworth-Heinemann. As was the case with the previous book, it is about fluid mechanics and the convective transport of heat (or any passive scalar quantity) for simple Newtonian, incompressible fluids, treated from the point of view of classical continuum mechanics. It is intended for a graduate-level course that introduces students to fundamental aspects of fluid mechanics and convective transport processes (mainly heat transfer and some single solute mass transfer) in a context that is relevant to applications that are likely to arise in research or industrial applications. In view of the current emphasis on small-scale systems, biological problems, and materials, rather than large-scale classical industrial problems, the book is focused more on viscous phenomena, thin films, interfacial phenomena, and related topics than was true 14 years ago, though there is still significant coverage of high-Reynolds-number and high-Peclet-number boundary layers in the second half of the book. It also incorporates an entirely new chapter on linear stability theory for many of the problems of greatest interest to chemical engineers.

   The material in this book is the basis of an introductory (two-term) graduate course on transport phenomena. It starts with a derivation of all of the necessary governing equations and boundary conditions in a context that is intended to focus on the underlying fundamental principles and the connections between this topic and other topics in continuum physics and thermodynamics. Some emphasis is also given to the limitations of both equations and boundary conditions (for example “non-Newtonian” behavior, the “no-slip” condition, surfactant and thermocapillary effects at interfaces, etc.). It should be noted, however, that though this course starts at the very beginning by deriving the basic equations from first principles, and thus can be taken successfully even without an undergraduate transport background, there are important topics from the undergraduate curriculum that are not included, especially macroscopic balances, friction factors, correlations for turbulent flow conditions, etc. The remainder of the book is concerned with how to solve transport and fluids problems analytically; but with a lot of emphasis on basic physics, scaling, nondimensionalization, and approximations that can be used to obtain solutions that are due either to geometric simplifications or large or small values of dimensionless parameters.


THE SCOPE OF THIS BOOK

No single book can encompass all topics, and the present book is no exception. We consider only laminar flows and transport processes involving laminar flows, for incompressible, Newtonian fluids. Specifically, we do not consider turbulent flows. We do not consider compressibility effects, nor do we consider numerical methods, except by means of a brief introduction to boundary integral techniques for creeping flows. Further, we do not consider non-Newtonian flows, except for a few limited homework examples, nor even the basic constitutive equations for non-Newtonian fluids except briefly in the introductory chapter, Chapter 2, primarily in the context of thinking about why fluids may exhibit non-Newtonian behavior and hence what the limitations of the Newtonian fluid approximation may be. We do consider both flow and convective transport processes, but with the latter generally posed as a heat transfer problem. We shall see, however, that much of the same analysis and principles apply to mass transfer when there is a single solute. Finally, multicomponent mass transfer is not considered, and in the graduate transport sequence of classes would often be taught as a separate class.

   The goal of this book is to provide a fundamental understanding of the governing principles for flow and convective transport processes in Newtonian fluids, and some of the modern tools and methods for “analysis” of this class of problems. By “analysis,” I mean both what one can achieve from a qualitative point of view without actually solving differential equations and boundary conditions, as well as detailed analytic solutions obtained generally from an asymptotic point of view. There is a strong emphasis on the derivation of basic equations and boundary conditions, including those relevant to a fluid interface. I also focus on complete descriptions of the solutions of representative problems rather than an exhaustive summary of all possible problems. This is because of the importance that I place on learning how to think about transport problems, and how to actually solve them, rather than just being told that some problem exists with a certain solution, but without adequate details to really understand how to achieve that solution or to generalize from the current problem to a related but presently unanticipated extension.

   An important tool that we develop in this book is the use of characteristic scales, nondimensionalization, and asymptotic techniques, in the analysis and understanding of transport processes. At the most straightforward level, asymptotic methods provide a systematic framework to generate approximate solutions of the nonlinear differential equations of fluid mechanics, as well as the corresponding thermal energy (or species transport) equations. Perhaps more important than the detailed solutions enabled by these methods, however, is that they demand an extremely close interplay between the mathematics and the physics, and in this way contribute a very powerful understanding of the physical phenomena that characterize a particular problem or process. The presence of large or small dimensionless parameters in appropriately nondimensionalized equations or boundary conditions is indicative of the relative magnitudes of the various physical mechanisms in each case, and is thus a basis for approximation via retention of the dominant terms.

   There is, in fact, an element of truth in the suggestion that asymptotic approximation methods are nothing more than a sophisticated version of dimensional analysis. Certainly it is true, as we shall see, that successful application of scaling/nondimensionalization can provide much of the information and insight about the nature of a given fluid mechanics or transport process without the need either to solve the governing differential equations or even be concerned with a detailed geometric description of the problem. The latter determines the magnitude of numerical coefficients in the correlations between dependent and independent dimensionless groups, but usually does not determine the form of the correlations. In this sense, asymptotic theory can reduce a whole class of problems, which differ only in the geometry of the boundaries and in the nature of the undisturbed flow, to the evaluation of a single coefficient. When the body or boundary geometry is simple, this can be done by means of detailed solutions of the governing equations and boundary conditions. Even when the geometry is too complex to obtain analytic solutions, however, the general asymptotic framework is unchanged, and the correlation between dimensionless groups is still reduced to determination of a single constant, which can now be done (in principle) by means of a single experimental measurement.

   It is important, however, not to overstate what can be accomplished by asymptotic (and related analytic) techniques applied either to fluid mechanics or heat (and mass) transfer processes. At most, these methods can treat limited regimes of the overall parameter domain for any particular problem. Furthermore, the approximate solutions obtained can be no more general than the framework allowed in the problem statement; that is, if we begin by seeking a steady axisymmetric solution, an asymptotic analysis will produce only an approximation for this class of solutions and, by itself, can guarantee neither that the solution is unique within this class nor that the limitation to steady and axisymmetric solutions is representative of the actual physical situation. For example, even if the geometry of the problem is completely axisymmetric, there is no guarantee that an axisymmetric solution exists for the velocity or temperature field, or if it does, that it corresponds to the motion or temperature field that would be realized in the laboratory. The latter may be either time dependent or fully three dimensional or both. In this case, the most that we may hope is that these more complex motions may exist as a consequence of instabilities in the basic, steady, axisymmetric solution, and thus that the conditions for departure from this basic state can be predicted within the framework of classical stability theories. The important message is that analytic techniques, including asymptotic methods, are not sufficient by themselves to understand fluid mechanics or heat transfer processes. Such techniques would almost always need to be supplemented by some combination of stability analysis or, more generally, by experimental or computational studies of the full problem.

   I want to thank my many colleagues and students who have contributed to this work for many years. I would also like to thank the users of the first edition who made substantial suggestions for improvement. I look forward to the reader’s reaction to this new version.

         L. Gary Leal
         Santa Barbara





Acknowledgments



I want to thank a number of people who contributed to this book. Most important among these were Professor G. M. Homsy, and several years of graduate students from my own classes at the University of California at Santa Barbara, who used this book in preprint form and provided much useful input on topics that required better explanation, typos, etc. In addition, these students had the first “opportunity” to work many of the problems at the end of each chapter, and this led to a number of important changes in the problem statements. I specifically appreciate their patience in this latter endeavor. I also owe a major debt of gratitude to number of faculty around the country, who had taught graduate transport classes from my previous book and provided detailed comments on the proposed contents and format of this new book. In addition, several of these individuals also contributed problems from their own classes, which they kindly allowed me to use in this new book. For this major contribution, I thank David Leighton from Notre Dame, John Brady from the California Institute of Technology, Roger Bonnecaze from the University of Texas at Austin, and James Oberhauser from the University of Virginia. In addition, Professor Howard Stone from Harvard University provided very useful notes on the dynamics of thin films from his own class, and also kindly read several of the new sections. Finally, I thank Cambridge University Press, and particularly Peter Gordon, for their patience in waiting for me to finish this book. The last 10 percent took at least 50 percent of the time! I take full responsibility for the contents of this book.





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