CHAPTER 1 INTRODUCTION - Universiti Teknologi Malaysiafkm.utm.my/~ummi/SME1313/Chapter 1.pdf ·...
Transcript of CHAPTER 1 INTRODUCTION - Universiti Teknologi Malaysiafkm.utm.my/~ummi/SME1313/Chapter 1.pdf ·...
SME 1313 Fluid Mechanics I
CHAPTER 1 INTRODUCTION
ByUmmikalsom Abidin
C24-316FKM, UTM
SME 1313 Fluid Mechanics I
IntroductionFluid Mechanics
Fluid Statics- fluid at rest
- deals with forces applied by fluids at rest
Fluid Dynamics- fluid in motion
Hydrostatic forces on submerged bodies
e.g dam, tanks storing fluid, automation actuators
Buoyant force applied by fluids on submerged or floating bodies
e.g ships, submarines
Hydrodynamics
e.g liquid flow in pipes and open channel (hydraulics), pumps,hydroturbines, water cooling system
Gas dynamics
e.g gas turbines, flow of air over a body (aerodynamics) –aircraft, rockets, automobiles
SME 1313 Fluid Mechanics I
Introduction
Naturally occuring flowsMeteorologyOceanographyHydrology
SME 1313 Fluid Mechanics I
What is fluid?Fluid is a substance that deforms continuously under the application of a shear (tangential) stress no matter how small the shear stress may be.
t1 t2
F Ft0
t2>t1>t0
(a) (b)
Behavior of (a) solid and (b) fluid, under the action of a constant shear
SME 1313 Fluid Mechanics I
What is fluid?
Fluids comprise the liquid and gas (or vapor) phases Distinction between solid,liquid and gas
StrongestMolecules are relatively fixed position
Solid
WeakestMolecules move about at random in the gas phase
Gas
ModerateGroups of molecules move about each other in the liquid phase
Liquid
Intermolecular bonds
Atom Arrangement
SME 1313 Fluid Mechanics I
What is fluid?Normal to surface
Force acting on area dA
Tangent to surface
Fn
dA Ft
Normal stress: σ = Fn/dA
Shear stress: ι = Ft/dA
The normal stress and shear stress at the surface of a fluid element. For fluids at rest, the shear stress is zero and the pressure is the only normal stress
SME 1313 Fluid Mechanics I
No-slip ConditionA fluid in direct contact with a solid “sticks” to the surface due to viscous effects, and there is no slip.The flow region adjacent to the wall in which the viscous effects(and thus the velocity gradients) are significant is called boundary layer.
Uniform approach
velocity, V
Relative velocities of
fluid layers
Zero velocity at the surface
Plate
A fluid flowing over stationary surface comes to a complete stopat the surface because of the no-slip condition
SME 1313 Fluid Mechanics I
Classification of Fluid FlowsViscous vs. Inviscid Regions of Flow
Viscous Flow Region – flows in which the frictional effect is significantInviscid Flow Region – viscous forces are negligibly small compared to inertial or pressure forces
Inviscid flow region
Viscous flow
region
Inviscid flow region
The flow of an originally uniform fluid stream over a flat plate, and the regions of viscous flow (next to the plate on both sides) and inviscid flow (away from the plate)
SME 1313 Fluid Mechanics I
Classification of Fluid Flows
Internal vs. External FlowInternal flow – flows in which the fluid is completely bounded by solid surface
e.g flow in a pipe or ductDominated by the influence of viscosity throughout the flow field
External flow – flows in which the fluid is unbounded over
solid surfacese.g flow over a plate, wire, sphere objectViscous effects are limited to boundary layers near solid surfaces and to wake regions downstream of bodies
* Open-channel flow – the flow of liquids in a duct in which the liquid is partially filled and there is a free surface e.g rivers, irrigation channels
SME 1313 Fluid Mechanics I
Classification of Fluid FlowsCompressible vs. Incompressible Flow
Incompressible Flow – density of the fluid remains nearly constant throughout
liquids, gases at low speedsdensity changes of gas flows are under 5% or when Ma<0.3
Compressible Flow – density changes of the fluid is significant
gases at high speedsdensity changes of gas flows are above 5% or when Ma>0.3
Mach number,Ma = V = Speed of flow
c Speed of soundMa=1 (Sonic), Ma<1 (Subsonic), Ma>1(Supersonic), Ma>>1 (Hypersonic)
(Speed of sound=346 m/s)
SME 1313 Fluid Mechanics I
Classification of Fluid FlowsLaminar vs. Turbulent Flow
In 1880s, Osborn Reynolds conducted an experiment to see flow patterns
Tank arranged as above with a pipe taking water from the centre into which dye is injected through a needle
SME 1313 Fluid Mechanics I
Classification of Fluid FlowsFilament of dye
Laminar (viscous)
Transitional
Turbulent
SME 1313 Fluid Mechanics I
Classification of Fluid Flows
Reynolds number,Re =ρud
µ
Laminar flow Re<2000Transitional flow 2000<Re<4000Turbulent flow Re>4000
SME 1313 Fluid Mechanics I
Classification of Fluid FlowsNatural (or unforced) vs. Forced Flow
Forced Flow – fluid is forced to flow over a surface or in a pipe by external means such as pump or a fanNatural Flow – any fluid motion is due to natural means such as buoyancy effect, where warmer (and thus lighter) fluid rises and cooler (and thus denser) fluid falls
Schlieren image of a hot water (left) and ice water (right) in a glass
SME 1313 Fluid Mechanics I
Classification of Fluid FlowsSteady vs. Unsteady Flow
Steady Flow – no change of fluid properties (velocity, pressure) at a point with time
Devices that are intended for continuous operation e.gturbines, pumps, boilers, condensers
Unsteady Flow – fluid properties change at a point with timeTransient – used for developing flows
t1=5 s
V1=10 m/s
t2=10 s
V2=10 m/s
t1=5 s
V1=10 m/s
t2=10 s
V2=11 m/s
SME 1313 Fluid Mechanics I
Classification of Fluid FlowsUniform vs. Non-uniform Flow
Uniform Flow – no change of fluid properties with location over a specified region
Non-uniform Flow – if at a given instant, fluid properties change with location over a specified region
V1=10 m/s V2=10 m/s
V1=10 m/s V2=11 m/s
or V=10 m/s
orV1=10 m/s
V2=10 m/s
1
2
2
1
SME 1313 Fluid Mechanics I
Classification of Fluid FlowsSteady uniform flow
Conditions do not change with position and with time e.g flow of water in a pipe of constant diameter at constant velocity
Steady non-uniform flowConditions change from point to point in the stream but do not change with time e.g flow in tapering pipe with constant velocity at inlet, but velocity change along the length of the pipe toward the exit
Unsteady uniform flowAt a given instant of time, the conditions at every point are the same, but will change with time e.g pipe of constant diameter connected to a pump pumping at a constant rate which is then switched off
Unsteady non-uniform flowEvery condition of the flow may change from point to point and with time at every point e.g waves in channel
SME 1313 Fluid Mechanics I
Classification of Fluid FlowsOne-, Two-, and Three-Dimensional Flows
1-D Flow – flow parameters (such as velocity, pressure, depth) vary in one primary dimensions2-D Flow - flow parameters vary in two primary dimensions3-D Flow - flow parameters vary in three primary dimensions
The development of the velocity profile in a circular pipe, V=V(r,z) and thus the flow is 2-D in the entrance region, and becomes 1-D downstream when the velocity
profile fully develops and remain unchanged in the flow direction, V=V(r)
z
Developing velocity profile, V(r,z)
Fully developed velocity profile, V(r)
r
SME 1313 Fluid Mechanics I
Classification of Fluid FlowsThe dimensionality of the flow also depends on the choice of coordinate system and its orientation
Rectangular coordinates, V(x,y,z)Cylindrical coordinates, V(r,θ,z)
Higher dimensionality should be considered if only very high accuracy is required
SME 1313 Fluid Mechanics I
Application Areas of Fluid Mechanics
Human body (Bio-fluid Mechanics)Cardiovascular system
Artificial heartPulmonary system
Breathing machine
BuildingWater supply systemSewerage systemHeating and air-conditioningAerodynamics forces and flow fields around structure
SME 1313 Fluid Mechanics I
Application Areas of Fluid Mechanics
AutomobilesHydraulic brakes, power steering, automatic transmissionFuels line, fuel pump, fuel injectorsLubrication systemsCooling systemsAir-conditioningAerodynamics design
AircraftAerofoil designGas turbine
SME 1313 Fluid Mechanics I
Application Areas of Fluid Mechanics
Ship, submarines, hovercraftHydrodynamics designBuoyancy and stability
IndustryCooling of electronicsAutomation system
RecreationalBadminton shuttle and golf ball aerodynamics
Geophysical fluid dynamicsMeteorologyOceanography
SME 1313 Fluid Mechanics I
System and Control VolumesSystem – quantity of matter or a region in space chosen for studySurroundings – mass or region outside the systemBoundary – Real or imaginary surface that separates the system from its surroundings (fixed or movable)
SYSTEM
SURROUNDINGS
BOUNDARY
SME 1313 Fluid Mechanics I
System and Control VolumesClosed System (Control Mass)
Consists of a fixed amount of mass, and no work, can cross the boundaryEnergy in the form of heat and work can cross the boundaryE.g piston-clinder device
Open System (Control Volume)Both mass and energy can cross the boundaryE.g compressor, turbine, nozzle, car radiator
Imaginary boundary
Real boundary
CV
(a nozzle) CV
Imaginary boundary
Imaginary boundary
SME 1313 Fluid Mechanics I
Dimensions and UnitsAny physical quantity can be characterized by dimensionsMagnitude assigned to the dimensions are called unitsPrimary or fundamental dimensions
mole (mol)Amount of matter
candela (cd)Amount of light
ampere (A)Electric of current
kelvin (K)Temperature
second (s)Time
kilogram (kg)Mass
meter (m)Length
UnitDimension
The seven fundamental (or primary) dimensions and their units in SI
SME 1313 Fluid Mechanics I
Dimensions and UnitsDerived or secondary dimensions are dimensions obtained from combination of primary dimensions
Most used derived dimensions
SME 1313 Fluid Mechanics I
SI UnitsMetric SI (from Le Systeme International d’Unites) or International SystemSI system was produced by General Conference of Weights and Measures in 1960SI is a simple and logical system and widely being used for scientific and engineering work in most of the industrialized nations
SME 1313 Fluid Mechanics I
SI Units
pico, p10-12
nano, n10-9
micro, µ10-6
milli, m10-3
centi, c10-2
deci, d10-1
deka, da101
hecto, h102
Kilo, k103
mega, M106
giga, G109
tera, T1012
PrefixMultiple
Standard prefixes in SI units
SME 1313 Fluid Mechanics I
Dimensional HomogeneityIn engineering, all equations must be dimensionally homogeneous where every term in an equation must have the same unit
SME 1313 Fluid Mechanics I
Problem-Solving TechniqueStep 1:Problem Statement
State briefly and concisely (in your own words) the information given and the quantities to be found
Step 2:SchematicDraw a schematic of the system or control volume to be used in the analysis.Indicate any energy and mass interactions with the surroundingsListing the given information on sketch
Step 3:Assumptions and ApproximationsState any assumptions and approximations made to simplify the problem to make it possible to obtain a solution
SME 1313 Fluid Mechanics I
Problem-Solving TechniqueStep 4:Physical Laws
Apply all the relevant basic physical laws and principle and reduce them to their simplest form by utilizing the assumptions made
Step 5:PropertiesDetermine the unknown properties at known states necessary to solve the problem from property relations or tables
Step 6:CalculationsSubstitute the known quantities into the simplified relations and perform the calculations to determine the unknownPay attention to the units and unit cancellationsGive appropriate number of significant digits
SME 1313 Fluid Mechanics I
Problem-Solving TechniqueStep 7:Reasoning, Verification, and Discussion
Check to make sure that the results obtained are reasonable and intuitive and verify the validity of the questionable assumptionsRepeat the calculations that resulted in unreasonable values