Fluid Mechanics and Energy Transport BIEN 301 Lecture 3 Viscosity, Flow Visualization, Flow Analysis Methods Juan M. Lopez, E.I.T. Research Consultant LeTourneau University Adjunct Lecturer Louisiana Tech University Viscosity Definition (White 1.7) Quantitative measure of a fluid’s resistance to flow. t u , In generalize d coordinate s g 2 u , In cartesian coordinate s, flat plane y 12/07/2006 BIEN 301 – Winter 2006-2007 Viscosity Newtonian vs. Non-Newtonian Fluids • Newtonian Fluids: Linear Viscosity Equation Examples? • Non-Newtonian Fluids: Non-linear Viscosity Eq. Examples? • Usually this difference is established as constant viscosity vs. non-constant viscosity. In ALL real fluids, however, viscosity can never be a true constant and varies with T and P. No-Slip Condition • For real fluids, it is assumed that at the boundaries, zero slip occurs. • This is due to jump balance across the interface. Temperature Balance Momentum Balance 12/07/2006 BIEN 301 – Winter 2006-2007 Viscosity Effects The principal effects of viscosity are divided into two readily visible areas: • The boundary layer formation • Turbulence We’ll cover boundary layer in greater depth later on. For now, we’ll focus on the second effect: generation of turbulence. We use a dimensionless number to correlate the effects of viscosity on a flow regime: the Reynolds Number. Re VL VL v where v 12/07/2006 BIEN 301 – Winter 2006-2007 Viscosity Effects Dimensionless Numbers Many dimensionless numbers in fluid mechanics. We will cover many, many of them throughout the quarter. Reynolds number relates the kinetic energy to the viscosity. • It helps us identify transition into turbulent region, where the viscosity is too great relative to the fluid motion, and orderly movement can no longer occur. Why dimensionless? • These are numbers that apply to a flow regime, related to a characteristic dimension. • Pick the characteristic dimension that better describes the region you are interested in studying, and apply the equation. 12/07/2006 BIEN 301 – Winter 2006-2007 Viscosity Effects Identify the characteristic dimension for each flow. 12/07/2006 BIEN 301 – Winter 2006-2007 Viscosity Effects It’s important to think carefully about the characteristic dimension, however it’s not absolutely a perfect science. You can pick an alternative characteristic dimension as long as you remain consistent as you compare systems 12/07/2006 BIEN 301 – Winter 2006-2007 Viscosity Effects Understanding the meaning of dimensionless numbers Even though they are quite an alien concept to people outside of fluid mechanics, it is important that you grasp these numbers and learn to obtain a “feel” for what these numbers are telling you. Reynolds number: • High Values, mean a high kinetic energy relative to its ability to flow. This should cause instability, therefore, we would expect turbulence. • Medium values, mean that the kinetic energy is smoothly related to its ability to flow. This should cause smoothly changing laminar flow. • Low values, mean a low kinetic energy related to its ability to flow. This would be a creeping flow where inertial effects are almost, if not entirely, negligible. 12/07/2006 BIEN 301 – Winter 2006-2007 Viscosity Effects - Example A standard example a moving plate with viscous fluid between the plate and a fixed surfaceVplate2 Vplate1 12/07/2006 BIEN 301 – Winter 2006-2007 Viscosity Changes Viscosity is dependent on temperature and pressure. For water, we can ignore the effects of pressure. Viscosity changes as a result of temperature are evident in all real fluids. For gases, we have two representations: Power Law and Sutherland Law: n T Power Law T0 3/ 2 0 T T S 0 T0 Sutherland Law T S 12/07/2006 BIEN 301 – Winter 2006-2007 Viscosity Changes For Liquids, the approximation is as follows: T0 T0 ln a b c T T 0 2 You can see how this gets much uglier very quickly. We really like idealized fluids. It’s unfortunate we don’t have more of them around. 12/07/2006 BIEN 301 – Winter 2006-2007 Thermal Effects Similar to viscosity, thermal conductivity changes the way heat transfer occurs within the fluid. Thermal conductivity acts on the temperature gradient present in the fluid to obtain a vector form of heat transfer 12/07/2006 BIEN 301 – Winter 2006-2007 Thermal Effects The gradient of a property is the partial differential of that property with respect to each of the principal dimensions of the field. Note the Del Operator is a vector operator. X X X X g1 , g 2 , g 3 , In generalize d coordinate s g1 g 2 g 3 T T T kT x, y, z k k k , for the thermal conductivi ty problem x y z 12/07/2006 BIEN 301 – Winter 2006-2007 Surface Tension Surface tension arises at the interface between a fluid and another system. This system can be another fluid, a solid, or nothing at all. Surface tension is a much more complicated subject than it will appear to be here. We will cover a simplified method of studying surface tension. 12/07/2006 BIEN 301 – Winter 2006-2007 Surface Tension The coefficient of surface tension, Υ, is a measure of force per unit length or energy per unit area present everywhere tangent to the surface, at the surface. Generally, Υ, changes with the same sign as temperature, reaching zero at a critical point. When the surface curves, the tension generates a pressure difference across the interface. 12/07/2006 BIEN 301 – Winter 2006-2007 Surface Tension The pressure across the surface interface can be expressed as follows: p , Pressure balance across a cylinder R 2 p , Pressure balance across a sphere R 4 p , Pressure balance across a hollow bubble R 12/07/2006 BIEN 301 – Winter 2006-2007 Surface Tension Wetting When a liquid interacts with a solid surface, there is an angle at that interaction. The magnitude of this angle defines whether an item wets the solid or not. • Water wets clean glass Water tends to sheet off clean glass, beads only with imperfections. • Water does not wet wax Water beading on the wax job of your car. 12/07/2006 BIEN 301 – Winter 2006-2007 Surface Tension Surface tension also causes the capillary effect. For a cylindrical capillary tube, the height of the fluid column that rises due to the surface tension and the material wetting the capillary can be found to be as follows: 2 cos h R 12/07/2006 BIEN 301 – Winter 2006-2007 Cavitation Cavitation is a function of vapor pressure. It can be highly damaging. Cavitation is described by a non-dimensional parameter, the cavitation number. Which is a function of Pa, ambient pressure, Pv, vapor pressure, and V, a characteristic velocity. p a pv Ca 1 2 V 2 12/07/2006 BIEN 301 – Winter 2006-2007 Cavitation For most fluids, there is a critical point for Ca below which the fluid will begin to cavitate. The spontaneous generation and rapid implosion of gas bubbles in the liquid can be a highly destructive force. If not monitored for appropriately, this can internally destroy a mechanical system. 12/07/2006 BIEN 301 – Winter 2006-2007 Speed of Sound Aside from cavitation, we can cause damage to pipes, ductwork, and cells when we start approaching flows that are a significant fraction of the speed of sound in that fluid. This produces damaging shock waves and erosion. This comes from the compressibility effects present in the fluid. For an ideal gas, the speed of sound is: a kRT 1/ 2 12/07/2006 BIEN 301 – Winter 2006-2007 Complicated Enough? The answer is…no. Not nearly enough. We have too many assumptions and simplifications. But this will allow us to begin working with fluids from a theoretical perspective. Our problems continue to complicate themselves…viscosity, then turbulence, now cavitation and compressibility-induced shock waves…it is apparent that a careful and engineered approach must be taken each and every time we deal with a flow system. Enough of the basics for now…how do we DEAL with a flow system? How do we visualize the results? How do we make sense of all of this stuff? 12/07/2006 BIEN 301 – Winter 2006-2007 Flow Visualization One of the most important tools in understanding fluid mechanics is being able to visualize what is going on in our system. When we visualize these flows, we often use one of a few standard visualization methods: 1) Streamline 3) Streakline 2) Pathline 4)Timeline Note that these are IDENTICAL in steady flow. 12/07/2006 BIEN 301 – Winter 2006-2007 Flow Visualizations Streamlines Everywhere tangent to the velocity vector at a given instant in time. dr dx dy dz V u v w 12/07/2006 BIEN 301 – Winter 2006-2007 Flow Visualizations Pathline The displacement of a particle over a defined period of time, defined by integrating its velocity vectors in time to obtain a path. t2 t2 t2 t1 t1 t1 x udt , y vdt, and z wdt 12/07/2006 BIEN 301 – Winter 2006-2007 Flow Visualizations Streaklines A streak line is a set of particles that has gone through a particular point in space. This is the way experimental work is generally collected. • Injecting hydrogen bubbles, smoke, etc. 12/07/2006 BIEN 301 – Winter 2006-2007 Flow Visualizations Timelines The set of particles that form a line in any given instant in time. Note that for all of these visualizations, streamlines are the “simple” ones to generate analytically. The rest are a result of experimentation. 12/07/2006 BIEN 301 – Winter 2006-2007 Flow Visualizations Check out the external links on blackboard to see some external references on flow visualizations. Whole careers are dedicated to the generation of adequate flow visualizations. Flow Visualization Example 12/07/2006 BIEN 301 – Winter 2006-2007 Flow Analysis Techniques Three primary methods of approaching a flow problem Integral Analysis (Control-Volume Approach) Differential Analysis (Infinitessimal Approach) Dimensional Analysis (Experimental Study) For ANY of these approaches, we must satisfy the basic laws of mechanics. 12/07/2006 BIEN 301 – Winter 2006-2007 Flow Analysis Techniques Flow Analysis Checklist: Conservation of Mass (Continuity, can also include conservation of species for mixtures) Conservation of Momentum (Newton’s second law) Conservation of Energy (First Law of Thermodynamics) A state relationship Adequate boundary conditions, initial conditions. Appropriate assumptions about our flow. 12/07/2006 BIEN 301 – Winter 2006-2007 Flow Analysis Techniques Assumptions Our principal assumptions sets come in pairs, to aid in describing our flow condition: • Steady or Unsteady? • Inviscid or Viscous? • Incompressible or Compressible? • Gas or Liquid? Once we’ve made our assumptions and followed the analysis checklist, we are more certain that our results will be meaningful. Coupled with White’s 1.13, this is a powerful approach to fluid mechanics. 12/07/2006 BIEN 301 – Winter 2006-2007 Assignment HW 3 has been posted on blackboard Project Proposals due next time! Individual project schedules are available on blackboard. 12/07/2006 BIEN 301 – Winter 2006-2007 Questions? 12/07/2006 BIEN 301 – Winter 2006-2007