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FLUID MECHANICS – 1 Semester 1 2011 - 2012 Week – 6 Class – 1 and 2 Bernoulli Equation Compiled and modified by Sharma, Adam
Review• Types of Motion - Translation, Deformation• Rotation• Vorticity• Existence of flow• Continuity equation• Irrotational flow
Objectives• Introduction• Definitions of Conservation Principles - Mass, momentum and energy• Conservation of mass principle• Mass balance under steady flow• Understand the use and limitations of the Bernoulli equation, and apply it to solve a variety of fluid flow problems.. 3
Wind turbine “farms” are being constructed all over the world toextract kinetic energy from the wind and convert it to electricalenergy. The mass, energy, momentum, and angular momentumbalances are utilized in the design of a wind turbine. TheBernoulli equation is also useful in the preliminary design stage. 4
INTRODUCTIONconservation laws refers to thelaws of1.conservation of mass,2. conservation of energy, and3.conservation of momentum.The conservation laws areapplied to a fixed quantity ofmatter called a closed system orjust a system, and then extendedto regions in space called controlvolumes.The conservation relations arealso called balance equationssince any conserved quantitymust balance during a process. 5
CHOOSING A CONTROL VOLUMEA control volume can be selected as any arbitraryregion in space through which fluid flows, and itsbounding control surface can be fixed, moving, andeven deforming during flow.Many flow systems involve stationary hardware firmlyfixed to a stationary surface, and such systems arebest analyzed using fixed control volumes.When analyzing flow systems that are moving ordeforming, it is usually more convenient to allow thecontrol volume to move or deform.In deforming control volume, part of the controlsurface moves relative to other parts. Examples of (a) fixed, (b) moving, and (c) deforming control 6 volumes.
FORCES ACTING ON A CONTROL VOLUMEThe forces acting on a control volume consist ofBody forces that act throughout the entire body of the controlvolume (such as gravity, electric, and magnetic forces) andSurface forces that act on the control surface (such as pressureand viscous forces and reaction forces at points of contact).Only external forces are considered in the analysis.Total force acting on control volume: The total force acting on a control volume is composed of body forces and surface forces; body force is shown on a differential volume element, and surface force is shown on a differential 7 surface element.
Conservation of MassThe conservation of mass relation for a closed system undergoing achange is expressed as msys = constant or dmsys/dt = 0, which is thestatement that the mass of the system remains constant during aprocess.Mass balance for a control volume (CV) in rate form: the total rates of mass flow into and out of the control volume the rate of change of mass within the control volume boundaries.Continuity equation: In fluid mechanics, the conservation ofmass relation written for a differential control volume is usuallycalled the continuity equation. 8
The Linear Momentum EquationLinear momentum: The product of the mass and the velocity of a bodyis called the linear momentum or just the momentum of the body.The momentum of a rigid body of mass m moving with a velocity V is m.Newton’s second law: The acceleration of a body is proportional to thenet force acting on it and is inversely proportional to its mass.The rate of change of momentum of a body is equal to the net forceacting on the body.Conservation of momentum principle: The momentum of a systemremains constant only when the net force acting on it is zero, and thusthe momentum of such systems is conserved.Linear momentum equation: In fluid mechanics, Newton’s second lawis usually referred to as the linear momentum equation. 9
ROTATIONAL MOTION AND ANGULAR MOMENTUMRotational motion: A motion duringwhich all points in the body move incircles about the axis of rotation.Rotational motion is described withangular quantities such as the angulardistance θ, angular velocity ω, andangular acceleration α.Angular velocity: The angulardistance traveled per unit time.Angular acceleration: The rate ofchange of angular velocity. The relations between angular distance θ, angular velocity ω , and linear velocity V. 10
Conservation of EnergyThe conservation of energy principle (the energy balance): Thenet energy transfer to or from a system during a process be equal tothe change in the energy content of the system.Energy can be transferred to or from a closed system by heat or work.Control volumes also involve energy transfer via mass flow. the total rates of energy transfer into and out of the control volume the rate of change of energy within the control volume boundariesIn fluid mechanics, we usually limit our consideration tomechanical forms of energy only. 11
CONSERVATION OF MASSConservation of mass: Mass, like energy, is a conservedproperty, and it cannot be created or destroyed during a process.Closed systems: The mass of the system remain constant duringa process.Control volumes: Mass can cross the boundaries, and so we mustkeep track of the amount of mass entering and leaving the controlvolume. Mass is conserved even during chemical reactions. Mass m and energy E can be converted to each other: c is the speed of light in a vacuum, c = 2.9979×108 m/s The mass change due to energy change is negligible. 12
Conservation of Mass PrincipleThe conservation of mass principle for a control volume: The net mass transferto or from a control volume during a time interval ∆t is equal to the net change(increase or decrease) in the total mass within the control volume during ∆t. the total rates of mass flow into and out of the control volume the rate of change of mass within the control volume boundaries. Mass balance is applicable to any control volume undergoing any kind of process. Conservation of mass principle 13 for an ordinary bathtub.
Mass Balance for Steady-Flow Processes During a steady-flow process, the total amount of mass contained within a control volume does not change with time (mCV = constant). Then the conservation of mass principle requires that the total amount of mass entering a control volume equal the total amount of mass leaving it. For steady-flow processes, we are interested in the amount of mass flowing per unit time, that is, the mass flow rate. Multiple inlets and exits Single stream Many engineering devices such as nozzles, diffusers, turbines, compressors, and pumps involve a single stream (only one inlet and one outlet).Conservation of mass principle for a two-inlet–one-outlet steady-flow system. 14
Special Case: Incompressible FlowThe conservation of mass relations can be simplified even further whenthe fluid is incompressible, which is usually the case for liquids. Steady, incompressible Steady, incompressible flow (single stream) There is no such thing as a “conservation of volume” principle. However, for steady flow of liquids, the volume flow rates, as well as the mass flow rates, remain constant since liquids are essentially incompressible substances. During a steady-flow process, volume flow rates are not necessarily conserved although mass flow rates are. 15
MECHANICAL ENERGY AND EFFICIENCYMechanical energy: The form of energy that can be converted tomechanical work completely and directly by an ideal mechanicaldevice such as an ideal turbine.Mechanical energy of a flowing fluid per unit mass: Flow energy + kinetic energy + potential energyMechanical energy change:• The mechanical energy of a fluid does not change during flow if its pressure, density, velocity, and elevation remain constant. 16
THE BERNOULLI EQUATIONBernoulli equation: An approximate relation between pressure,velocity, and elevation, and is valid in regions of steady,incompressible flow where net frictional forces are negligible.Despite its simplicity, it has proven to be a very powerful tool in fluidmechanics.The Bernoulli approximation is typically useful in flow regions outsideof boundary layers and wakes, where the fluid motion is governed bythe combined effects of pressure and gravity forces. The Bernoulli equation is an approximate equation that is valid only in inviscid regions of flow where net viscous forces are negligibly small compared to inertial, gravitational, or pressure forces. Such regions occur outside of boundary layers and wakes. 17
Acceleration of a Fluid ParticleIn two-dimensional flow, the acceleration can be decomposed into twocomponents:streamwise acceleration as along the streamline andnormal acceleration an in the direction normal to the streamline, which isgiven as an = V 2/R.Streamwise acceleration is due to a change in speed along a streamline,and normal acceleration is due to a change in direction.For particles that move along a straight path, an = 0 since the radius ofcurvature is infinity and thus there is no change in direction. The Bernoulliequation results from a force balance along a streamline. During steady flow, a fluid may not accelerate in time at a fixed point, Acceleration in steady but it may accelerate in space. flow is due to the change 18 of velocity with position.
Derivation of the Bernoulli Equation Steady flow: Bernoulli Steady, incompressible flow: The forces acting on a fluid equation particle along a streamline.The sum of the kinetic, potential, and The Bernoulli equation between anyflow energies of a fluid particle is two points on the same streamline:constant along a streamline duringsteady flow when compressibility andfrictional effects are negligible. 19
The incompressible Bernoulli equation is derived assuming incompressible flow, and thus it should not be used for flows with significant compressibility effects.The Bernoulli equation for unsteady, compressible flow: 21
• The Bernoulli equation can be viewed as the “conservation of mechanical energy principle.” • This is equivalent to the general conservation of energy principle for systems that do not involve any conversion of mechanical energy and thermal energy to each other, and thus the mechanical energy and thermal energy are conserved separately. • The Bernoulli equation states that during steady, incompressible flow with negligibleThe Bernoulli equation friction, the various forms of mechanicalstates that the sum of the energy are converted to each other, but theirkinetic, potential, and flow sum remains constant.energies of a fluid particle is • There is no dissipation of mechanical energyconstant along a streamline during such flows since there is no friction thatduring steady flow. converts mechanical energy to sensible thermal (internal) energy. • The Bernoulli equation is commonly used in practice since a variety of practical fluid flow problems can be analyzed to reasonable accuracy with it. 22
Example 5-5: Spraying Waterinto the AirA child use his thumb to cover most of thehose outlet, causing a thin jet of high-speedwater to emerge.The pressure in the hose just upstream ofhis thumb is 400kPa. If the hose is heldupward, what is the maximum height of thejet. 23
Example 5-6: Water Discharge from aLarge TankA large tank open to atmosphere isfilled with water to a height of 5m fromthe outlet tap. Then the tap is opened,and water flows out from the outlet.Determine the maximum watervelocity at the outlet. 24
Example 5-7: Siphoning OutGasoline from a Fuel TankThe difference in pressure betweenpoint 1 and point 2 causes fuel toflow. Point 2 is located 0.75mbelow point 1. The siphon diameteris 5mm, and frictional losses isdisregarded.Determine,a)Minimum time to withdraw 4L offuel from the tankb)The pressure at point 3.Take density of fuel is 750kg/m3.Patm=1 atm=101.3kPa. 25
Static, Dynamic, and Stagnation PressuresThe kinetic and potential energies of the fluid can be converted to flowenergy (and vice versa) during flow, causing the pressure to change.Multiplying the Bernoulli equation by the density gives1. P is the static pressure2. ρ V2/2 is the dynamic pressure3. ρ gz is the hydrostatic pressureTotal pressure: The sum of the static, dynamic, and hydrostaticpressures. Therefore, the Bernoulli equation states that the totalpressure along a streamline is constant. 27
Stagnation pressure: The sum of the static and dynamic pressures. It representsthe pressure at a point where the fluid is brought to a complete stop.Stagnation streamline The static, dynamic, and stagnation pressures measured using piezometer tubes. 28
Limitations on the Use of the Bernoulli Equation1. Steady flow The Bernoulli equation is applicable to steady flow.2. Frictionless flow Every flow involves some friction, no matter how small, and frictional effects may or may not be negligible.3. No shaft work The Bernoulli equation is not applicable in a flow section that involves a pump, turbine, fan, or any other machine or impeller since such devices destroy the streamlines and carry out energy interactions with the fluid particles. When these devices exist, the energy equation should be used instead.4. Incompressible flow Density is taken constant in the derivation of the Bernoulli equation. The flow is incompressible for liquids and also by gases at Mach numbers less than about 0.3.5. No heat transfer The density of a gas is inversely proportional to temperature, and thus the Bernoulli equation should not be used for flow sections that involve significant temperature change such as heating or cooling sections.6. Flow along a streamline The Bernoulli equation is applicable along a streamline. However, when a region of the flow is irrotational and there is negligibly small vorticity in the flow field, the Bernoulli equation becomes applicable across streamlines as well. 29
Frictional effects, heat transfer, and components that disturb the streamlined structure of flow make the Bernoulli equation invalid. It should not be used in any of the flows shown here.When the flow is irrotational, the Bernoulli equation becomes applicable 30between any two points along the flow (not just on the same streamline).
Hydraulic Grade Line (HGL) and Energy Grade Line (EGL)It is often convenient to represent the level of mechanical energy graphically usingheights to facilitate visualization of the various terms of the Bernoulli equation.Dividing each term of the Bernoulli equation by g gives P/ρ g is the pressure head; it represents the height of a fluid column that produces the static pressure P. V2/2g is the velocity head; it represents the elevation needed for a fluid to reach the velocity V during frictionless free fall. z is the elevation head; it represents the potential energy of the fluid. Bernoulli equation is expressed in terms of heads as: The sum of the pressure, velocity, and elevation heads is constant along a streamline. In Fluid Mechanics, head is a concept that relates the energy of fluid to the height of column of the fluid 31
Hydraulic grade line (HGL), P/ρ g + z The line that represents the sum ofthe static pressure and the elevation heads.Energy grade line (EGL), P/ρ g + V2/2g + z The line that represents thetotal head of the fluid.Dynamic head, V2/2g The difference between the heights of EGL and HGL. The hydraulic grade line (HGL) and the energy grade line (EGL) for free discharge from a reservoir through a horizontal pipe with a diffuser. 32
Notes on HGL and EGL• For stationary bodies such as reservoirs or lakes, the EGL and HGL coincide with the free surface of the liquid.• The EGL is always a distance V2/2g above the HGL. These two curves approach each other as the velocity decreases, and they diverge as the velocity increases.• In an idealized Bernoulli-type flow, EGL is horizontal and its height remains constant.• For open-channel flow, the HGL coincides with the free surface of the liquid, and the EGL is a distance V2/2g above the free surface.• At a pipe exit, the pressure head is zero (atmospheric pressure) and thus the HGL coincides with the pipe outlet.• The mechanical energy loss due to frictional effects (conversion to thermal energy) causes the EGL and HGL to slope downward in the direction of flow. The slope is a measure of the head loss in the pipe. A component, such as a valve, that generates significant frictional effects causes a sudden drop in both EGL and HGL at that location.• A steep jump/drop occurs in EGL and HGL whenever mechanical energy is added/removed to/from the fluid (pump/turbine).• The (gage) pressure of a fluid is zero at locations where the HGL intersects the fluid. The pressure in a flow section that lies above the HGL is negative, and the pressure in a section that lies below the HGL is positive. 33
In an idealized Bernoulli-type flow,EGL is horizontal and its height A steep jump occurs in EGL and HGLremains constant. But this is not whenever mechanical energy is added tothe case for HGL when the flow the fluid by a pump, and a steep dropvelocity varies along the flow. occurs whenever mechanical energy is removed from the fluid by a turbine. The gage pressure of a fluid is zero at locations where the HGL intersects the fluid, and the pressure is negative (vacuum) in a flow section that lies 34 above the HGL.
Example: Water Discharge Example:from a Large Tank Spraying Water into the Air 35
Example: Siphoning OutGasoline from a Fuel Tank 36
Example: Velocity Measurementby a Pitot Tube 37
Summary• Introduction Principle of conservation of Mass, Momentum and Energy• Conservation of Mass Conservation of Mass Principle Mass Balance for Steady-Flow Processes Special Case: Incompressible Flow• Mechanical Energy and Efficiency• The Bernoulli Equation Acceleration of a Fluid Particle Derivation of the Bernoulli Equation Static, Dynamic, and Stagnation Pressures Limitations on the Use of the Bernoulli Equation Hydraulic Grade Line (HGL) and Energy Grade Line (EGL) Applications of the Bernouli Equation 38