A semi-bounded fluid stream in thermal nonequilibrium with its bounding solid surface exchanges heat by surface convection qku and this alters its temperature (and qk and qu) only in a region adjacent to the bounding surface (i.e., the farfield temperature is unchanged). In this chapter we consider a steady, semi-bounded fluid stream flowing over a solid surface (e.g., flow over a plate or a sphere) at a far-field velocity uf,∞ with the solid Ts and the far-field Tf,∞ fluid having different temperatures. We initially focus on the fluid and its motion and heat transfer adjacent to the surface (because of this focus, the chapter title, semi-bounded fluid streams, is used. Also as will be shown, there are some similarities with the transient conduction in semi-infinite solid). Later we include the heat transfer with any bounding solid (i.e., the substrate). This is also called external flow heat transfer. In Chapter 7 we will consider steady, bounded fluid streams (e.g., flow in a tube). This is also called internal flow. We are interested in the parameters and conditions influencing the surface-convection heat flux qku and its spatial variation. These parameters and conditions include the direction of the fluid flow with respect to the bounding surface (e.g., fluid flow parallel to the surface, perpendicular to the surface, or oblique), flow structure, fluid properties, liquid-gas phase change, and solid-surface conditions.

A typical one-semester course syllabus is given in the Solutions Manual. However, at the discretion of the instructor, different parts of the text can be chosen to emphasize various concepts.

Chapter 1 is, in part, descriptive (as opposed to quantitative) and introduces many concepts. Therefore, this chapter should be read for a qualitative outcome and an overview of the scope of the book. This is needed for a general discussion of heat transfer analysis before specifics are introduced. The drawing of heat flux vector tracking is initially challenging. However, once learned, it facilitates visualization of heat transfer, and then the construction of the thermal circuit diagrams becomes rather easy.

Also, to get a broad and unified coverage of the subject matter, a very general treatment of spatial temperature nonuniformity and the appropriate form of the energy equation is given in Chapter 2. This chapter gives the building blocks and the results to be used in succeeding chapters. Some of the energy conversion mechanisms may be new to students; however, they are described in the text and are easy to follow. Application of Chapter 2 materials unfolds in the chapters that follow. For example, various energy conversion mechanisms are used along with heat transfermechanisms in interesting and practical problems.

Introduction

When a fluid is locally perturbed by an impulse (for example, by an impact) or a periodic excitation (the vibration of a membrane, string, or mechanical blade), the perturbation may propagate from the source in the form of a wave. Examples include acoustic waves, surface waves, and internal waves in a stratified fluid (Lighthill, 1978). The solution of the linearized equations for small amplitude perturbations leads to a major result: the wave number k and frequency ω (or the wave speed c = ω/k) are not independent, they are related by a dispersion relation. Since this relation is obtained from linearized equations, another major result is that dispersion does not depend on the amplitude of the perturbation. However, if the amplitude exceeds some level, new effects arise that the dispersion relation of linear theory obviously does not describe. To explain these new effects it is necessary to include nonlinear terms neglected in the linear study, i.e., to develop a theory of nonlinear waves. Such waves are also referred to as finite-amplitude waves, in contrast to the waves of infinitesimal amplitude considered in a linear analysis.

The objective of the present chapter is to give an elementary account of the theory of nonlinear waves. We will show (i) how nonlinear waves can be constructed by a perturbation method (essentially the multiple-scale method presented in the preceding chapter), and (ii) how the linear stability of these waves can be studied.

Introduction

In this chapter we present an introduction to dense granular flows and their stability by discussing two classes of phenomena: avalanches on an inclined plane, and particle transport on an erodible bed sheared by a fluid flow. These granular flows lead to the appearance of surface waves, called ripples or dunes depending on whether their wavelength is of a few centimeters or a few meters (the relevance of this common distinction will be discussed later on). Owing to the difficulty – both experimental and theoretical – of studying granular media, the mechanisms responsible for these waves remain poorly understood, and so the results presented in this chapter are definitely less well established than those in the preceding chapters.

Avalanches, ripples, and dunes present serious problems for human activities. Among natural phenomena, snow and mud avalanches are well known for their destructive nature; the displacement of a sand dune by the wind – the so-called aeolian dunes – while less dramatic, can cut communication links and threaten habitation and industrial installations. Subaqueous dunes perturb navigation in rivers and shallow seas such as the North Sea, while on river bottoms such dunes increase friction and raise the water level, thereby contributing to flooding. Granular flows are also omnipresent in industry: flow and transport of coal, construction materials (cement, sand, gravel), agricultural foodstuffs, pharmaceutical materials, and sand from oilfields are some examples. Instabilities occur in the conduits used to transport these materials, giving rise to dunes which perturb the flow and may form obstructions, causing serious damage to operating equipment.

Hydrodynamic instabilities occupy a special position in fluid mechanics. Since the time of Osborne Reynolds and G. I. Taylor, it has been known that the transition from laminar flow to turbulence is due to the instability of the laminar state to certain classes of perturbations, both infinitesimal and of finite amplitude. This paradigm was first displayed in a masterful way in the studies of G. I. Taylor on the instability of Couette flow generated by the differential rotation of two coaxial cylinders. From then on, the theory of hydrodynamical instability has formed a part of the arsenal of techniques available to the researcher in fluid mechanics for studying transitions in a wide variety of flows in mechanical engineering, chemical engineering, aerodynamics, and in natural phenomena (climatology, meteorology, and geophysics).

The literature on this subject is so vast that very few researchers have attempted to write a pedagogical text which describes the major developments in the field. Owing to the enormity of the task, there is a temptation to cover a large number of physical situations at the risk of repetition and of wearying the reader with just a series of methodological approaches. François Charru has managed to avoid this hazard and has risen to the challenge. With this book he fills the gap between the classical texts of Chandrasekhar and Drazin and Reid, and the more recent book of Schmid and Henningson.

Classical instability theory essentially deals with quasi-parallel or parallel shear flows such as mixing layers, jets, wakes, Poiseuille flow in a channel, boundary-layer flow, and so on.

Introduction

When a viscous flow has a deformable interface, small inertial effects can give rise to an instability which is manifested as interfacial waves. The principal types of such flows are illustrated in Figure 6.1: liquid films falling down an inclined plane, flows induced by a pressure gradient, and shear flows.

Falling films composed of a single layer (Figure 6.1a) or of several layers (Figure 6.1b) are often encountered in coating processes. Examples are coating of paints and varnishes, printing inks, magnetic tape and disks, photographic film, and so on. Flows set in motion by a pressure gradient (Figure 6.1c) are encountered in extrusion of polymers in planar or annular geometries. The third type of flow, shear flow, typically corresponds to a liquid film sheared by a gas (Figure 6.1d), a situation encountered in chemical reactors or heat exchangers, or by Marangoni stresses. In these applications it is often required that the films have uniform thickness, and so it is essential to avoid instabilities. On the other hand, instabilities may actually be desirable because they typically augment rates of heat and mass transfer.

Figure 6.2 illustrates an instability observed in the oil industry in the transport of oil of very high viscosity on the order of a million times that of water. Water, which is injected into the pipe in order to reduce the viscous friction, migrates to the wall where it forms a lubricating film (Joseph et al., 1997).

Introduction

In this chapter we discuss how various gravitational, capillary, and thermal phenomena can initiate an instability in a fluid initially at rest. In such a motionless fluid, advection of momentum plays a negligible role in the small amplitude theory, unlike the situations that will be studied in later chapters. We also present the basic techniques for studying linear stability: derivation of the equations for small perturbations of a base state, linearization, and determination of the normal modes and the dispersion relation.

An important part of this chapter is devoted to the analysis of problems in terms of ratios of characteristic scales. The approach we take is to simplify the problem by evaluating the order of magnitude of the involved phenomena before embarking on long analytic or numerical calculations. This allows us to retain only the most important effects and to elucidate mechanisms. This dimensional analysis, which is essential in both fundamental and applied research, is often sufficient for determining the scaling laws governing the problem. It allows the choice of a set of suitable reference scales to recast the problem in dimensionless form, or, in other words, to recast the problem in a system of units composed of scales that are intrinsic to the problem. This modeling approach then guides the later calculations, for example, by revealing a small parameter which suggests an asymptotic expansion. It also serves to justify or reject a posteriori certain hypotheses, and leads to a better understanding of the physics of the problem.

In this appendix we shall derive a system of depth-averaged conservation equations, the classic Saint-Venant equations (de Saint-Venant, 1871), which give a good description of the dynamics of a fluid flow when the spatial scale λ of the variations in the longitudinal direction x is large compared to the flow depth or thickness, h. These equations do not explicitly involve the nature of the flowing medium, and so they are valid, under certain conditions stated explicitly below, for a fluid flow either laminar or turbulent, as well as for a granular flow. The equations can be obtained by two equivalent methods: by depth-averaging the local conservation equations in the transverse direction, or by writing down the conservation laws for a control volume corresponding to a slice of fluid of thickness dx. Here we shall use the latter method.

Outflow from a slice of fluid

Let us consider a flow in the x-direction, inclined at an angle θ relative to the horizontal, between a bed located at y = yb(x, t), where y is the transverse direction, and a free surface at y = (yb + h)(x, t), where h is the local flow depth (Figure A.1).

We define the control volume as the slice of fluid between the two planes at x and x + dx. At any point on the boundary of the control volume, let n be the exterior normal, u the fluid velocity and w the speed of the boundary.

Introduction

An instability typical of a parallel flow was demonstrated in an experiment performed by Osborne Reynolds (1883) and repeated by Thorpe (1969). A horizontal long tube is filled carefully with a layer of water lying on top of a layer of heavier colored brine (salt water), as sketched in Figure 4.1a. The tube is suddenly tipped several degrees: the brine falls and the water rises, creating a shear flow which displays an inflection point near the interface (Figure 4.1b). In a few seconds a wave of sinusoidal shape develops at the interface of the two fluids, and leads to regular co-rotating vortices, as shown in Figure 4.2. These vortices are a manifestation of the Kelvin–Helmholtz instability. This instability owes its origin to the inertia of the fluids; viscosity plays only a minor role, tending to attenuate the growth of the wave only slightly by momentum diffusion.

Another manifestation of the Kelvin–Helmholtz instability on a much larger atmospheric scale is illustrated in Figure 4.3. An upper air layer flows over a lower layer moving more slowly, with different humidity and temperature. The thin layer of clouds formed at the interface displays billows which are the exact analogs of those in Figure 4.1. Figure 4.4 shows another example, in a mixing layer formed between a flow of water on the left and a flow of water and air bubbles on the right.