Fluid Mechanics Flashcards
Mechanics -
Mechanics - physical science that deals with both stationary and moving bodies under the influence of forces.
The branch of mechanics that deals with bodies at rest is called statics, while the branch that deals with bodies in motion is called dynamics.
Fluid mechanics -
Fluid mechanics is the science that deals with the behaviour of fluids at rest (fluid statics) or in motion (fluid dynamics), and the interaction of fluids with solids or other fluids at the boundaries.
Hydrodynamics -
Hydraulics -
The study of the motion of fluids that are practically incompressible (such as liquids, especially water, and gases at low speeds) is usually referred to as hydrodynamics.
A subcategory of hydrodynamics is hydraulics, which deals with liquid flows in pipes and open channels.
Gas dynamics
Aerodynamics
Propulsion
Meterology
Oceonography
Hydrology
Gas dynamics deals with the flow of fluids that undergo significant density changes, such as the flow of gases through nozzles at high speeds.
The category aerodynamics deals with the flow of gases (especially air) over bodies such as aircraft, rockets, and automobiles at high or low speeds.
Propulsion (Internal Flows)
Meterology
Oceonography
Hydrology
stress -
types
Fluid -
a fluid at rest is at a state of ______ shear stress
No-slip condition -
Boundary Layer -
Flow separation -
No temp. jump -
Brief History of Fluid Mechanics
stress - resistance developed as a result of applied force
tangential or shear stress
Normal stress
Fluid - Substance that continues to undergo deformation no matter how small the shear force is applied.
a fluid at rest is at a state of zero shear stress
No-slip condition - relative velocity of fluid in contact with solid is zero because of viscosity
Boundary Layer - the region near the surface where viscosity effects are significant
Flow separation - in regions of adverse pressure gradient flow separates from surface
No temp. jump - a fluid and a solid surface have the same temperature at the points of contact
Fluid Flow Classification
Viscous Flow vs Inviscid Flow
Internal Flows vs External Flows -
Laminar Flow vs Turbulent Flow - Natural vs Forced Flow - Steady Flows vs Unsteady Flows Uniform Vs Non-uniform
System, Boundary Closed system (Control Mass System), Open System (Control Volume)
Fluid Flow Classification
Viscous Flow vs Inviscid Flow
Internal Flows vs External Flows - flow is completely bounded vs flow is unbounded
Laminar Flow vs Turbulent Flow -
Natural vs Forced Flow - like flow due to buoyancy effects vs flow due to fan
Steady Flows vs Unsteady Flows
Uniform Vs Non-uniform
System, Boundary Closed system (Control Mass System), Open System (Control Volume)
Experimental approach -
Analytical Approach -
Accuracy -
Precision -
Property -
Intensive -
Extensive -
State of a system -
Continuum -
Specific properties -
Specific weight -
Specific gravity -
EOS -
at ______ pressure and _____ temperature gas behaves as ideal gas
Experimental approach - expensive, time-consuming & often impractical but closest approximation to reality within limits of experimental error
Analytical Approach - fast, inexpensive but accuracy depends on assumptions & model used
Accuracy - nearness to true value
Precision - repeatability
Property - any characteristic of a system
Intensive - nature of system on mass/extent of system P, T
Extensive - mass of system not on nature m, V
State of a system - The number of properties required to fix the state of a system is given by the state postulate: The state of a simple compressible system is completely specified by two independent, intensive properties.
Continuum - a continuous, homogeneous matter with no spacing, that is, a continuum
Specific properties - per unit mass
Specific weight - rho-g
Specific gravity - ratio of density of fluid to that of water or air
EOS - equation that relates P, T & rho
like Ideal gas equation
at low pressure and high-temperature gas behaves as ideal gas
Saturation T -
Saturation P -
Vapour Pressure -
Partial Pressure -
Cavitation -
One to one correspondence between P & T during phase change process
Saturation T - At a given pressure, the temperature at which a pure substance changes phase is called the saturation temperature T sat .
Saturation P - At a given temperature, the pressure at which a pure substance changes phase is called the saturation pressure P sat.
Vapour Pressure - the pressure exerted by a vapor in phase equilibrium with its liquid, at a given temperature.
Partial Pressure - Partial pressure is defined as the pressure of a gas or vapor in a mixture with other gases
The rate of evaporation from open water bodies such as lakes is controlled by the difference between the vapor pressure and the partial pressure.
Cavitation - when the pressure in liquid-flow systems drops below the vapor pressure at some locations (tip of impeller or suction sides of pumps) it results in vaporization and formation of bubbles, which are swept away from the low-pressure regions and on collapsing generates highly destructive high-pressure waves. It is a common cause for drop-in performance and even the erosion of impeller blades.
Energy -
Microscopic energy -
internal energy of a system.
Macroscopic energy -
Mechanical energy
Heat -
Sensible energy -
Latent energy -
calorie (1 cal = 4.1868 J) -
Simple Compressible Systems -
Energy - exist in various forms such as thermal, mechanical, kinetic, potential, electrical, magnetic, chemical, and nuclear
Microscopic energy - energy related to the molecular structure and the degree of the molecular activity of a system.
Thermal (sensible, latent), chemical, Nuclear energy
The sum of all microscopic forms of energy is called the internal energy of a system.
Macroscopic energy - related to motion and influence of external effects such as gravity, magnetism, electricity.
K.E, P.E
Mechanical energy (flow+k.e+p.e) - can be converted to mechanical work Heat - energy transfer due to temp. difference Sensible energy - that portion of internal energy associated with the activeness of molecules & is proportional to temperature Latent energy - that portion of internal energy associated with the molecular arrangement or phase change
calorie (1 cal = 4.1868 J) - energy needed to raise the temperature of 1 g of water at 14.5°C by 1°C.
Simple Compressible Systems - absence of magnetic, electric and surface tension effects
Bulk modulus of elasticity or coefficient of compressibility -
Isothermal compressibilty (alpha) (inverse of Coefficient of Compressibility) -
Water hammer -
Coefficient of Volume expansion (beta) -
Bulk modulus of elasticity or coefficient of compressibility - change in pressure corresponding to fractional change in volume at constant T. Infinite for incompressible fluid Isothermal compressibilty (alpha) (inverse of Coefficient of Compressibility) - fractional change in volume corresponding to a unit change in pressure for constant T
Water hammer - when fluid flow encounters abrupt flow restriction (such as sudden closure of valve) it is locally compressed producing acoustic waves which resemble the sound produced when a pipe is hammered. It is very dangerous & can even damage the pipeline.
Coefficient of Volume expansion (beta) - fractional change in volume corresponding to unit change in T at const P
viscosity -
Newtonian fluid -
The viscosity of liquids _______ and the viscosity of gases ______ with increase in temperature
kinetic theory of gases predicts the viscosity of gases to be proportional to the _____________
surface tension -
why liquid droplets take spherical shape.
capillary effect -
if cohesive forces _____ than adhesive forces - fall in capillary height, contact angle will be _____ 90 degree
viscosity - internal resistance of a fluid to motion. cohesive forces between molecules & molecular momentum transfer
Newtonian fluid - stress is proportional to strain rate
The viscosity of liquids decreases and the viscosity of gases increases with increase in temperature
kinetic theory of gases predicts the viscosity of gases to be proportional to the square root of temperature
surface tension - the surface of the liquid acts like a stretched elastic membrane under tension due to cohesive forces between the molecules.
Net attractive force acting on the molecule at the surface of the liquid tends to pull them towards the interior of the liquid thereby compressing them which causes the liquid to minimize its surface area. For a given volume min. surface area is that of a sphere so liquid droplets take spherical shape.
capillary effect - the rise or fall of a liquid in small-diameter tube inserted into the liquid
if cohesive forces greater than adhesive forces - fall in capillary height, contact angle will be >90
if cohesive forces less than adhesive forces - rise in capillary height, contact angle will be <90
Pressure -
Pressure is the _______ force per unit area, & is a ______________
Absolute Pressure -
Gauge Pressure -
Vacuum pressure -
Pressure at a point -
Pascal’s Law -
Pressure measuring devices -
Barometer -
Atmospheric pressure values -
Pressure - normal force exerted by a fluid per unit area
Pressure is the compressive force per unit area, & is a scalar
Absolute Pressure - actual pressure at a given position is called the absolute pressure, and it is measured relative to absolute vacuum (i.e., absolute zero pressure)
Gauge Pressure - difference between absolute pressure and local atmospheric pressure
Vacuum pressure - pressure below atmospheric pressure & is the difference between atmospheric pressure & absolute pressure
Pressure at a point - the pressure at a point in a fluid has the same magnitude in all directions (from force balance)
Variation of pressure with depth - rhogh (this principle used in manometer)
Pascal’s Law - the pressure applied to a confined fluid increases the pressure throughout by the same amount
Hydraulic brakes & lifts are based on this principle
Pressure measuring devices - manometer, bourdon tube, pressure transducers
Barometer - measures atmospheric pressure
Atmospheric pressure values - 1.01325 bar, 101.325 kPa, 1 atm, 760mm of Hg, 760 torr are same. 1 bar = 100kPa
Fluid statics -
Hydrostatic forces on submerged plane surfaces -
centre of pressure -
Hydrostatic forces on submerged curved surfaces
Buoyancy -
Archimedes principle -
Fluid statics - forces on fluid at rest (no shear force only pressure force)
Hydrostatic forces on submerged plane surfaces -
The magnitude of the resultant force acting on a plane surface of a completely submerged plate in a homogeneous (constant density) fluid is equal to the product of the pressure Pc at the centroid of the surface and the area A of the surface.
centre of pressure - intersection between line of action of resultant force and surface
Hydrostatic forces on submerged curved surfaces
- The horizontal component of the hydrostatic force acting on a curved surface is equal (in both magnitude and the line of action) to the hydrostatic force acting on the vertical projection of the curved surface.
- The vertical component of the hydrostatic force acting on a curved surface is equal to the hydrostatic force acting on the horizontal projection of the curved surface, plus (minus, if acting in the opposite direction) the weight of the fluid block.
Buoyancy - fluid exerts an upward force on a body immersed in it that tends to lift the body
The buoyancy force is caused by the increase of pressure in a fluid with depth
Weight of the fluid displaced by the fluid
It is independent of the density of solid and its distance from free surface.
Archimedes principle - The buoyant force acting on a body immersed in a fluid is equal to the weight of the fluid displaced by the body, and it acts upward through the centroid of the displaced volume.
Stability
stable -
neutrally stable -
unstable -
stability of immersed body
inherently stable in the vertical direction
rotational stability of an immersed body depends on the relative locations of the center of gravity G of the body and the center of buoyancy B (i.e centroid of displaced volume)
stable
unstable
neutrally stable
What about a case where the center of gravity is not vertically aligned with the center of buoyancy ?
Stability
stable - any small disturbance generates a restoring force that returns it to its initial position.
neutrally stable - if someone moves the ball, it would stay at its new location. It has no tendency to move back to its original location, nor does it continue to move away
unstable - any disturbance, even an infinitesimal one, body does not return to its original position; rather it diverges from it.
stability of immersed body
For an immersed or floating body in static equilibrium, the weight and the buoyant force acting on the body balance each other, and such bodies are inherently stable in the vertical direction
rotational stability of an immersed body depends on the relative locations of the center of gravity G of the body and the center of buoyancy B (i.e centroid of displaced volume)
centre of G is directly below centre of Buoyancy - stable
a stable design for a submarine calls for the engines and the cabins for the crew to be located at the lower half in order to shift the weight to the bottom as much as possible. Hot-air or helium balloons (which can be viewed as being immersed in air) are also stable since the cage that carries the load is at the bottom
center of gravity G is directly above point B - unstable
A body for which G and B coincide - neutrally stable
What about a case where the center of gravity is not vertically aligned with the center of buoyancy (Fig. 3–45)? It is not really appropriate to discuss stability for this case since the body is not in a state of equilibrium. In other words, it cannot be at rest and would rotate toward its stable state even without any disturbance.
stability for floating body metacentric height metacentre - stable - unstable -
Fluids in rigid body motion
rotation of cylinder -
stability for floating body
measure of stability for floating bodies is the metacentric height GM
distance between the center of gravity G and the metacenter M
metacentre - the intersection point of the lines of action of the buoyant force through the body before and after rotation
stable - if point M is above point G i.e GM +ve
unstable - if point M is below point G i.e GM -ve
a boat can tilt to some maximum angle (20 degree) without capsizing, but beyond that angle, it overturns (and sinks)
Fluids in rigid body motion
- eg transportation in tankers or rotation of cylinder (no motion between fluid layers relative to each other)
- equation of motion for rigid body
- acceleration on a straight path
- free surface & const. pressure lines are parallel inclined surfaces
rotation of cylinder - forced vortex motion
- equations of motion
- free surface and constant pressure lines are paraboloids of revolution
Fluid kinematics -
Lagrangian approach -
Eulerian approach -
Flow field - Pressure, Velocity & Acceleration fields
convective term - (V.del)
total or material derivative (D/Dt) - local (del/delt) + convective (V.del)
Flow visualization
streamlines -
streamtube -
Pathline -
streaklines -
For a steady flow streamline, pathline & streakline are identical but can be quite different for unsteady flow
Main difference is that a streamline _________, while a streakline and a pathline _____________
Timeline -
Fluid kinematics - deals with describing the motion of fluids without necessarily considering the forces and moments that cause the motion
Lagrangian approach - particle-based approach to study
Eulerian approach - region-based approach or control volume based approach
Flow field - Pressure, Velocity & Acceleration fields
convective term - (V.del)
total or material derivative (D/Dt) - local (del/delt) + convective (V.del)
Flow visualization
streamlines - A streamline is a curve tangent to which gives the local velocity vector at that instant
streamtube - bundle of streamlines
Streamlines are useful indicators of the direction of fluid motion throughout the flow field at an instant e.g, regions of recirculating flow
and separation of a fluid off of a solid wall are easily identified by the streamline pattern. Streamlines cannot be directly observed experimentally
except in steady flow fields, in which they are coincident with pathlines and streaklines
Pathline - actual path traversed by fluid particle
A modern experimental technique called particle image velocimetry (PIV) utilizes particle pathlines to measure the velocity field over an entire
plane in a flow. In PIV, tiny tracer particles are suspended in the fluid & flow field is inferred from them using photography & computers
streaklines - locus of all particles that have previously passed through same location by introducing dye or smoke we get streaklines smoke wire (thin wire coated with mineral oil which breaks into beads due to surface tension & on applying current results in streakline of smoke)
For a steady flow streamline, pathline & streakline are identical but can be quite different for unsteady flow
Main difference is that a streamline represents flow pattern at a given instant in time, while a streakline and a pathline are flow patterns that have a time history associated with them.
Timeline - set of adjacent fluid particles marked at the same instant in time
Timelines are particularly useful in situations where the uniformity of a flow (or lack thereof) is to be examined
Hydrogen bubble wire (experimentally in a water channel) - when electric current is passed through the wire, electrolysis of the water occurs and tiny hydrogen gas bubbles form at the wire
Refractive Flow Visualization Techniques -
shadowgraph technique -
schlieren technique -
Interferometry -
Kármán vortex street -
Plots of fluid flow data -
profile plot -
vector plots -
contour plot -
Types of motion or Deformation of fluid elements
- strain rate tensor Vorticity and Rotationality Rotational flow - - circular flows may be \_\_\_\_\_\_\_\_ fluid in boundary layer region is \_\_\_\_\_\_\_\_ & outside it is \_\_\_\_\_\_\_\_\_\_\_\_
Thus if a flow originates in an irrotational region, it remains irrotational until some ______ process alters it.
solid body rotation
line vortex
Reynolds Transport Theorem -
Refractive Flow Visualization Techniques - based on the refractive property i.e the light rays bend as they travel from one medium to another owing to a difference in index of refraction. used where density changes from one location in the flow to another, such as natural convection flows (temperature differences cause the density variations), mixing flows (fluid species cause the density variations), and supersonic flows (shock waves and expansion waves cause the density variations).
shadowgraph technique -
schlieren technique -
Interferometry - visualization technique that utilizes the phase change of light as it passes through air of varying densities
Kármán vortex street - unsteady vortices shed in an alternating pattern, in a flow past the cylinder
Plots of fluid flow data -
profile plot - indicates how the value of a scalar property varies along some desired direction in the flow field.
vector plots - an array of arrows indicating the magnitude and direction of a vector property at an instant in time.
contour plot - shows curves of constant values of a scalar property (or magnitude of a vector property) at an instant in time.
vector plot - gives both magnitude & direction unlike streamlines that give direction only
contour plots - quickly reveal regions of high (or low) values of the flow property being studied
Types of motion or Deformation of fluid elements
- translation, rotation, linear strain & shear strain
- as fluid elements may be in constant motion, motion & deformation is described using rates.
- rate of translation (velocity, V)
- rate of rotation (angular velocity, omega)
- linear strain rate (epsilonxx, yy, zz), volumetric strain rate (zero for incompressible flow)
- shear strain rate
- strain rate tensor (a combination of linear strain rate and shear strain rate into one symmetric second-order tensor)
Vorticity and Rotationality
vorticity - curl of V ( a measure of rotation of a fluid particle)
- it is twice the angular velocity
Rotational flow - if vorticity is non-zero
- circular flows may be rotational
fluid in boundary layer region is rotational & outside it is irrotational
The vorticity of a fluid element cannot change except through the action of viscosity, nonuniform heating (temperature gradients), or other
nonuniform phenomena. Thus if a flow originates in an irrotational region, it remains irrotational until some nonuniform process alters it.
solid body rotation (v=wr) - circular streamlines, flow is rotational (as vorticity is non-zero) [roundabout] line vortex (v=k/r) - circular streamlines, flow is irrotaional (as vorticity is zero) [ferris wheel]
Reynolds Transport Theorem - RTT relates the rates of change of an extensive property between a closed system and for a control volume system.
Ch.5 Mass, Bernoulli & Energy Equations
conservation of mass -
conservation of mass relation written for differential control volume is continuity equation
Newton’s second law of motion -
conservation of momentum -
conservation of energy -
del - used for path function that have____ differentials like heat, work & mass transfer
d - for point functions that have ____differentials
A simple rule in selecting a control volume is to make the control surface _______ toflow at all locations whereit crosses fluid flow, whenever possible.
some practical application like syringe involve deforming CV
mechanical energy -
mechanical energy of a fluid ( __+__+__ ) does not change during flow ifits ____, ____, ____, and _____ remain constant. In the absenceof any losses, the mechanical energy change represents the mechanicalwork supplied to the fluid or extracted from the fluid.
The transfer of mechanical energy is usually accomplished by a ________, and thus mechanical work is often referred to as _________.
A pump or a fan receives ___ (usually from an electric motor) and transfers itto the fluid as ____ energy (less frictional losses).
A turbine, on the other hand, converts the ___ energy of a fluid to ____ work.
conservation of mass - mass of system remains constant during a process
conservation of mass relation written for differential control volume is continuity equation
Newton’s second law of motion - rate of change of momentum of a body is equal to net force acting on the body
conservation of momentum - net force is zero, momentum is conserved.
conservation of energy - net energy transfer to or from a system during a process be equal to the change in the energy content of the system
del - used for path function that have inexact differentials like heat, work & mass transfer
d - for point functions that have exact differentials
A simple rule in selecting a control volume is to make the control surface normal to flow at all locations where it crosses fluid flow, whenever possible.
some practical application like syringe involve deforming CV
mechanical energy - the form of energy that can be converted to mechanical work completely and directly by an ideal mechanical device such as an ideal turbine. Kinetic and potential energies are the familiar forms of mechanical energy. Thermal energy is not mechanical energy, however, since it cannot be converted to work directly and completely (the second law of thermodynamics)
mechanical energy of a fluid (flow energy+k.e+p.e) does not change during flow if its pressure, density, velocity, and elevation remain constant. In the absence of any losses, the mechanical energy change represents the mechanical work supplied to the fluid or extracted from the fluid.
The transfer of mechanical energy is usually accomplished by a rotating shaft, and thus mechanical work is often referred to as shaft work. A pump
or a fan receives shaft work (usually from an electric motor) and transfers it to the fluid as mechanical energy (less frictional losses). A turbine, on the
other hand, converts the mechanical energy of a fluid to shaft work.
Bernoulli equation - in mechanical energy terms
Bernoulli equation - in pressure head terms
Limitations of Bernoulli’s equation -
static pressure (P) - Dynamic pressure (rhoV^2/2) - stagnation pressure (Pstag)- Hydrostatic pressure (rhogz) -
Piezometer tube -
Pitot static tube -
Bernoulli equation - The mechanical energy ( i.e sum of the kinetic, potential, and flow energies) of a fluid particle is constant along a streamline for a steady, incompressible and frictionless flow
Bernoulli equation - the sum of total pressure ( i.e static, dynamic & hydrostatic pressure) is constant along a streamline.
Limitations of Bernoulli’s equation - steady flow, frictionless flow, no shaft work & no heat transfer, incompressible flow & flow along a streamline
static pressure (P) - actual thermodynamic pressure, it doesn't incorporate any dynamics effects Dynamic pressure (rhoV^2/2) - pressure rise when fluid brought to rest isentropically stagnation pressure (Pstag)- sum of static plus dynamic pressure Hydrostatic pressure (rhogz) - it accounts for elevation effects
If static and stagnation pressure of a flowing liquid are greater than atmospheric pressure, a vertical transparent tube called a piezometer tube (or simply a piezometer) can be attached to the pressure tap and to the Pitot tube.
Piezometer tube - measures static pressure for +ve gauge pressure of flowing liquid
Pitot static tube - directly measures dynamics pressure
Bernoulli equation - in terms of Mechanical energy
Bernoulli equation - in terms of pressure energy
Limitations of Bernoulli’s equation -
static pressure -
Dynamic pressure -
stagnation pressure -
Hydrostatic pressure -
If static and stagnation pressure of a flowing liquid are greater than atmospheric pressure, a vertical transparent tube called a piezometer tube (or simply a piezometer) can beattached to the pressure tap and to the Pitot tube.
Piezometer tube -
Pitot static tube - directly measures dynamics pressure
Bernoulli Equation - in terms of head
Hydraulic Grade Line -
Energy Grade Line -
For stationary bodies such as reservoirs or lakes, the EGL and HGL_____ with the free surface of the liquid. The elevation of the freesurface z in such cases represents _____ the EGL and the HGL since thevelocity is ____ and the static pressure (gage) is ____
The EGL is always a distance _____ above the HGL. These two linesapproach each other as the velocity _____, and they diverge as thevelocity _____. The height of the HGL decreases as the velocity______, and vice versa.
In an idealized Bernoulli-type flow, EGL is _____ and its height(or not) remains _____. This would also be the case for HGL when the flowvelocity is ______
The mechanical energy loss due to frictional effects (conversion tothermal energy) causes the EGL and HGL to slope______ in thedirection of flow
For open-channel flow, the HGL coincides with the free surface of theliquid, and the EGL is a distance ____ above the free surface
At a pipe exit, the pressure head is zero (atmospheric pressure) and thusthe HGL ____ with the pipe outlet
A _____ occurs in EGL and HGL whenever mechanical energy isadded to the fluid (by a pump, for example). Likewise, a ____occurs in EGL and HGL whenever mechanical energy is removed fromthe fluid (by a turbine, for example)
The pressure (gage) of a fluid is _____ at locations where the HGLintersects the fluid. The pressure in a flow section that lies above the HGLis _____, and the pressure in a section that lies below the HGL is_____
first law of thermodynamics -
The energy content of a fixed quantity of mass (a closed system) can bechanged by ____ mechanisms:
Thermal Energy -
Heat -
work -
shaft work
work done by pressure forces
Bernoulli Equation - The sum of the pressure, velocity, and elevation heads along a streamline is constant for steady, incompressible & frictionless flows
why heads used - convenient to represent the level of mechanical energy graphically using heights to facilitate visualization of the various terms of the Bernoulli equation
static Pressure head - P/rhog
velocity head - v^2/2g
elevation head - z
Hydraulic Grade Line - The line that represents the sum of the static pressure and the elevation heads.
Energy Grade Line - The line that represents the total head of the fluid
For stationary bodies such as reservoirs or lakes, the EGL and HGL coincide with the free surface of the liquid. The elevation of the free surface z in such cases represents both the EGL and the HGL since the velocity is zero and the static pressure (gage) is zero
The EGL is always a distance V^2/2g above the HGL. These two lines approach each other as the velocity decreases, and they diverge as the velocity increases. The height of the HGL decreases as the velocity increases, and vice versa.
In an idealized Bernoulli-type flow, EGL is horizontal and its height remains constant. This would also be the case for HGL when the flow velocity is constant
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
For open-channel flow, the HGL coincides with the free surface of the liquid, and the EGL is a distance V^2/2g above the free surface
At a pipe exit, the pressure head is zero (atmospheric pressure) and thus the HGL coincides with the pipe outlet
A steep jump occurs in EGL and HGL whenever mechanical energy is added to the fluid (by a pump, for example). Likewise, a steep drop (Horizontal) occurs in EGL and HGL whenever mechanical energy is removed from the fluid (by a turbine, for example)
The pressure (gage) 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
first law of thermodynamics (conservation of energy principle) - Energy can neither be created nor be destroyed during a process; it can only change forms.
The energy content of a fixed quantity of mass (a closed system) can be changed by two mechanisms: heat transfer Q and work transfer W
Thermal Energy - sensible & latent forms of internal energy
Heat - energy transfer by virtue of temperature difference. The direction of Heat transfer is always from higher temp to lower temp.
work - energy interaction associated with a force acting through a distance. A rising piston, a rotating shaft, and an electric wire crossing the
system boundary are all associated with work interactions.
shaft work
work done by pressure forces
Ch.8 Flow in Pipes
Why fluids, especially liquids, are transported in circular pipes.?
Laminar & Turbulent Flow
Reynolds Number -
Critical Reynolds Number value -
Hydraulic Diameter -
Transition from Laminar to Turbulent flow also depends on -
In Most practical conditions Transition regime
In Pipe flow -
in Boundary layer -
laminar flow can be maintained at much higher Reynolds numbers (______) in very smooth pipes by avoidingflow disturbances and pipe vibrations.
Entrance Region -
Entrance Length Formula - for laminar & for turbulent
Laminar flow in Pipes -
Turbulent flow in Pipes -
terms such as -
Unlike laminar flow, the expressions for the velocity profile in a turbulentflow are based on both __________
the velocity profile is parabolic in laminarflow but is much fuller in turbulent flow, with a sharp drop near the pipewall. Turbulent flow along a wall can be considered to consist of fourregions ______, characterized by the distance from the wall.
Colebrook equation -
Moody chart -
Vena contracta -
Minor Losses -
Losses more in sudden contraction or sudden expansion?
Piping Network & Pump Selection -
Flow rate & Velocity Measurements -
Obstruction Flowmeters:
Positive Displacement Flow meters
Why fluids, especially liquids, are transported in circular pipes.?
Pipes with a circular cross-section can withstand large pressure differences between the inside and the outside without undergoing significant distortion. Noncircular pipes are usually used in applications such as the heating and cooling systems of buildings where the pressure difference is relatively small.
Laminar & Turbulent Flow
Reynolds Number - Ratio of Inertia force to Viscous force
Critical Reynolds Number value - depends on geometry & flow conditions
Hydraulic Diameter - Dh=4A/P
Transition from Laminar to Turbulent flow also depends on - surface roughness, pipe vibrations, and fluctuations in the flow
In Most practical conditions Transition regime
In Pipe flow - 2300 - 4000
in Boundary layer - 10^6
laminar flow can be maintained at much higher Reynolds numbers (upto 10^5) in very smooth pipes by avoiding flow disturbances and pipe vibrations.
Entrance Region - The region beyond the entrance region in which the velocity profile is fully developed and remains unchanged is called the hydrodynamically fully developed region. The flow is said to be fully developed when the normal-
ized temperature profile remains unchanged as well.
Entrance Length Formula - for laminar & for turbulent
Laminar flow in Pipes -
Turbulent flow in Pipes -
terms such as - rho_u’v’ & rho_u’2 called Reynolds shear stresses
Eddy motion and thus eddy diffusivities are much larger than their molecular counterparts in the core region of a turbulent boundary layer. The eddy motion loses its intensity close to the wall and diminishes at the wall because of the no-slip condition (uЈ and vЈ are identically zero at a stationary wall). Therefore, the velocity profile is very slowly changing in the core region of a turbulent boundary layer, but very steep in the thin layer adjacent to the wall, resulting in large velocity gradients at the wall surface. So it is no surprise that the wall shear stress is much larger in turbulent flow than it is in laminar flow
Unlike laminar flow, the expressions for the velocity profile in a turbulent flow are based on both analysis and measurements, and thus they are semi-empirical in nature with constants determined from experimental data.
the velocity profile is parabolic in laminar flow but is much fuller in turbulent flow, with a sharp drop near the pipe wall. Turbulent flow along a wall can be considered to consist of four regions (VBOT), characterized by the distance from the wall.
(V) Viscous sublayer - (0 - 5 wall units) law of the wall
very thin layer next to wall, viscous effects are dominant, velocity profile in this layer is very nearly linear, and flow is streamlined
(B) Buffer layer -
Next to the viscous sublayer, turbulent effects are becoming significant, but the flow is still dominated by viscous effects.
(O) Overlap layer - logarithmic law
Above the buffer layer, in which the turbulent effects are much more significant, but still not dominant.
(T) Turbulent layer -
Above the transition layer, turbulent effects dominate over viscous effects.
Colebrook equation - implicit relation obtained by curve fitting exercise on experimental data of friction factor dependence on Re & relative roughness
Moody chart - used to obtain friction factor values for relative roughness & Reynold values
Vena contracta - the point in a fluid stream where the diameter of the stream is the least, and fluid velocity is at its maximum
It is formed as fluid streamlines can’t change direction abruptly.
The streamlines are unable to closely follow the sharp angle in the pipe/tank wall. The converging streamlines follow a smooth path, which results in the narrowing of the jet.
Minor Losses -
Losses more in sudden contraction or sudden expansion?
sudden expansion because of flow separation.
Piping Network & Pump Selection -
Flow rate & Velocity Measurements -
Pitot and Pitot-Static Probes
Obstruction Flowmeters: Orifice, Venturi, and Nozzle Meters
Positive Displacement Flow meters
Ch.9 Differential Analysis of Fluid Flow
Control Volume Technique -
Differential analysis -
Conservation of mass -
Stream function -
Conservation of Linear momentum -
Navier-Stokes Equation -
Differential Analysis of Fluid flow -
Some flow types -
Couette flow -
Poiseuille flow -
Creeping flow -
Potential flow -
Ch.9 Differential Analysis of Fluid Flow
Control Volume Technique - control volume technique is useful when we are interested in the overall features of a flow, such as mass flow rate into and out of the control volume ornet forces applied to bodies.
The interior of the control volume is in fact treated like a “black box” in control volume analysis—we cannot obtain detailed knowledge about flow properties such as velocity or pressure at points inside the control volume.
Differential analysis, on the other hand, involves application of differentialequations of fluid motion to any and every point in the flow field over a regioncalled the flow domain.When solved, these differentialequations yield details about the velocity, density, pressure, etc., at every pointthroughout the entire flow domain.
Conservation of mass -
Stream function -
Conservation of Linear momentum -
Navier-Stokes Equation -
Differential Analysis of Fluid flow -
Some flow types -
Couette flow - flow between two parallel plates
Poiseuille flow - flow inside a pipe or channel
Creeping flow - inertial terms are negligible
Potential flow - inviscid & irrotational flow
Ch.10 Approximate Solutions of N-S equations
Ch.10 Approximate Solutions of N-S equations
Ch.11 Flow over Bodies: Drag & Lift
Two Dimensional flow -
Axisymmetric flow -
Bluff body -
Streamlined shape -
DRAG AND LIFT
A stationary fluid exerts only _______ forces on the surface of abody immersed in it.
A moving fluid, however, also exerts __________
forces on the surface because of the _______
Drag force -
Lift force -
The fluid forces also may generate moments and cause the body to rotate.
Rolling moment -
Yawing moment -
Pitching moment -
Drag formula & Lift formula
Thedrag and lift coefficients are primarily functions of the shape of the body, but in some cases, they also depend on the Reynolds number and the surfaceroughness
terminal velocity &
Ch.11 Flow over Bodies: Drag & Lift
Two Dimensional flow -The flow over a body is said to be two-dimensionalwhen the body is very long and of constant cross-section and the flow isnormal to the body.
The two-dimensional idealization is appropriate when the body is sufficiently long so that the end effects are negligible and the approach flow is
uniform.
Axisymmetric flow - when the body possesses rotationalsymmetry about an axis in the flow direction. The flow in this case is alsotwo-dimensional and is said to be axisymmetric.
Bluff body - Body (such as a building) tends to blockthe flow and is said to be bluff or blunt.
Streamlined shape - shapes having smooth changes in shape
DRAG AND LIFT
The force a flowing fluid exerts on a bodyalong the flow directionis called drag.
A stationary fluid exerts only normal pressure forces on the surface of abody immersed in it. A moving fluid, however, also exerts tangential shear
forces on the surface because of the no-slip condition caused by viscouseffects.
Drag force - the drag force is due to the combined effects of pressure andwall shear forces in the flow direction
Lift force - The components of the pressure andwall shear forces in the direction normal to the flow is called lift.
For two-dimensional flows, the resultant of the pressure and shear forcescan be split into two components: one in the direction of flow, which is the
drag force, and another in the direction normal to flow, which is the lift.
For three-dimensional flows, there is also a side forcecomponent in the direction normal to the page
The fluid forces also may generate moments and cause the body to rotate.
Rolling moment - The moment about the flow direction is called the rolling moment
Yawing moment - themoment about the lift direction is called the yawing moment, and
Pitching moment - themoment about the side force direction is called the pitching moment.
Drag formula & Lift formula
it is found convenient to work with appropriate dimensionless numbers that represent the drag and lift characteristics of the body. These numbers are the drag coefficient C D , and the lift coefficient C L
Thedrag and lift coefficients are primarily functions of the shape of the body, but in some cases, they also depend on the Reynolds number and the surfaceroughness
the maximum velocity a falling body can attain and iscalled the terminal velocity & all the forcesbalance each other and the net force acting on the body (and thus its acceleration) is zero. The forces acting on a falling body are usually the drag force, the buoyant force, and the weight of the body