MP211 Lec-1
Transcript of MP211 Lec-1
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MP 211 - FLUID MECHANICS
2013/2014
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COURSE CONTENT
Building a Fluid Mechanics Vocabulary
Fluid Properties Fluid Statics
Pressure Measurement
Fluid Forces
Newtonian and non-Newtonian fluids
Fluids in Motion
Conservation of Mass: Continuity Equation
Conservation of Energy, Part I: Bernoulli’s Equation
Conservation of Momentum: Momentum Equation
Conservation of Energy, Part II: Energy Equation
Application of the Basic Principles
Hydraulic Modeling
Flow of fluids in circular and non-circular Pipes
Flow of fluids in open channels
Pumps and pump characteristics
Energy Losses
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INTRODUCTION
Fluid mechanics is the study of the behavior of
fluids , either at rest (fluid statics) or in motion (fluid
dynamics)
Fluid is defined as a substance that deforms
continuously when acted on by a shearing stress of
any magnitude.
Fluids can be either liquids or
gases Liquids e.g. Water, gasoline, and
alcohol
Gases e.g. Air, water vapour,
oxygen, nitrogen, methane etc
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LIQUID VS GAS
A liquid takes the shape of thecontainer it is in and forms a
free surface in the presence of
gravity
A gas expands until itencounters the walls of the
container and fills the entire
available space. Gases cannot
form a free surface
Gas and vapor are often used
as synonymous words
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5
HISTORY
Faces of Fluid Mechanics
Archimedes(C. 287-212 BC)
Newton(1642-1727)
Leibniz(1646-1716)
Euler(1707-1783)
Navier(1785-1836)
Stokes(1819-1903)
Reynolds(1842-1912)
Prandtl(1875-1953)
Bernoulli(1667-1748)
Taylor
(1886-1975)
http://www-gap.dcs.st-and.ac.uk/~history/PictDisplay/Taylor_Geoffrey.html
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DIMENSIONS AND UNITS
Any physical quantity canbe characterized bydimensions.
The magnitudes assignedto dimensions are calledunits.
Primary dimensions (orfundamental dimensions)include: mass M , length L,time T , and temperature Ɵ,etc .
By General Conference of Weights and
Measures
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DIMENSIONS AND UNITS
For a wide variety of problems involving fluid
mechanics, only the three basic dimensions, L, T ,
and M are required. Alternatively, L, T , and F could
be used, where F is the basic dimensions of force
Quantity Name of unit SI - Unit symbol
Length (L) meter m
Mass (m) kilogram kg or (N.s2 /m)
Time (T ) second s
Temperature (ɵ) Kelvin K
Force (F ) Newton N or (kg.m/s2 )
Note: equivalent unit of F = ma = kg.m/s 2
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DIMENSIONS AND UNITS
Secondary dimensions (derived dimensions) can be expressed interms of primary dimensions and include: area (A), pressure (P),velocity V , energy E , and volume V, etc...
e.g. Area= length × length =L 2 = m 2
Velocity = Distance/time = L/T = m/s
Unit systems include; English system or U.S. Customary system and
Metric SI (International System)
All theoretically derived equations describing physical phenomenaare dimensional ly homogeneous
Equation:
Dimension:
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DIMENSIONS AND UNITS
Homogeneity of an equation;
general homogeneous equat ions : valid in any system of
units
restr ic ted h omogeneous equat ions: valid only to a
particular system of units
E.g. an equation for the distance, d, traveled by a freely falling
body can be expressed as;
, OR ...........????
Show the dimensions of the above equations!!
What is your observation?
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DIMENSIONS AND UNITS
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DIMENSIONS AND UNITS Based on the notational scheme introduced in 1967,
The degree symbol was officially dropped from the absolutetemperature unit,
All unit names were to be written without capitalization even if theywere derived from proper names (Table 1 –1).
However, the abbreviation of a unit was to be capitalized if the unit was
derived from a proper name. For example, the SI unit of force, which isnamed after Sir Isaac Newton (1647 –1723), is newton (not Newton),and it is abbreviated as N.
Also, the full name of a unit may be pluralized, but its abbreviationcannot. For example, the length of an object can be 5 m or 5 meters,not 5 ms or 5 meter.
Finally, no period is to be used in unit abbreviations unless they appearat the end of a sentence. For example, the proper abbreviation ofmeter is m (not m.).
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DIMENSIONS AND UNITS
Unit systemsSI Units
In SI, the units of mass, length, and time are the kilogram (kg),
meter (m), and second (s), respectively.
Bri t ish Gravi tat ional (BG) System
The unit of length is the foot (ft), the time unit is the second (s), the
force unit is the pound (lb)
The unit of mass is slug and it is derived from from Newton’s second
law F = ma
m=F/a = lb/(ft/s2) = lb.s2 /ft = slug
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DIMENSIONS AND UNITS
English Engineering (EE) Units In English or U.S customary system, the units of mass,
length, and time are the pound-mass (lbm), foot (ft), and
second (s), respectively
The unit of force is pound (lb or lbf) Force and mass are defined independently
Special care is required while using these parameters
in conjunction with Newton’s second law
Is “ 1lbm= 1 slug” ????
1lbm = 0.45359 kg
1ft = 0.3048 m
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DIMENSIONS AND UNITS
Force Units and relation between lbm and slug
SI :
EE:
BG :
We call a mass of 32.174 lbm 1 slug
For the EE system, a 1-lb force is defined as that force which givesa 1lbm a standard acceleration of gravity which is taken as
32.2ft/s2
A dimensionally homogeneous Newton’s second law is expressed
as
where, g c is propotionality constrant
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DIMENSIONS AND UNITS
Pressure is defined as the amount of force exerted on a unit area ofa substance
Pam
N
area
force
P
2
Pressure is compressive normal force applied by the fluid to the
surface
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DIMENSIONS AND UNITS
Consider a force, , acting on a 2D region of area
A sitting on x-y plane
Cartesian components:
F
x
y
z
F
F F i F j F k
x y z ( ) ( ) ( )
A
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C ARTESIAN COMPONENTS i
F z
F x
j
k
- Unit vector in x-direction
- Unit vector in y-direction
- Unit vector in z-direction
- Magnitude of in x-direction (tangent to surface) F
F y - Magnitude of in y-direction (tangent to surface)
- Magnitude of in z-direction (normal to surface)
F
F
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F
A shear stress
x( )
- For simplicity, let F y 0
• Pressure and Shear stress
p F
A
normal stress pressure z
( ( ))
• Shear stress and pressure at a point
F
A
x
Alim 0
p F
A
z
A
lim 0
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DIMENSIONS AND UNITS
Pascals’ laws:
Pressure acts uniformly in all directions ona small volume (point) of a fluid
In a fluid confined by solid boundaries,
pressure acts perpendicular to the
boundary – it is a normal force.
More on pressure...
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DIMENSIONS AND UNITS
Furnace duct Pipe or tube
Heat exchanger
Dam
Pressure is a Normal Force
(acts perpendicular to surfaces)
It is also called a Surface Force
Direction of fluid pressure on boundaries
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DIMENSIONS AND UNITS
Unit Definition or
Relationship
1 pascal (Pa) 1 kg m-1
s-2
1 bar 1 x 105 Pa
1 atmosphere (atm) 101,325 Pa
1 torr 1 / 760 atm760 mm Hg 1 atm
14.696 pounds per
sq. in. (psi)
1 atm
Units for Pressure
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DIMENSIONS AND UNITS
Weight, W is a force. It is the gravitational force applied to a body,and its magnitude is determined from Newton’s second law ,
where m is the mass of the body, and g is the local gravitationalacceleration (g is 9.807 m/s2 or 32.174 ft/s2
The weight of a unit volume of a substance is called the specificweight, g and is determined from;
or where r is density, V is volume
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DIMENSIONS AND UNITS
Work , which is a form of energy, can simply be defined asforce times distance; therefore, it has the unit “newton-meter
(N . m),” which is called a joule (J). That is,
A more common unit for energy in SI is the kilojoule (1 kJ =103 J). In the English system, the energy unit is the Btu
(British thermal unit), which is defined as the energy required
to raise the temperature of 1 lbm of water at 68°F by 1°F.
In the metric system, the amount of energy needed to raise
the temperature of 1 g of water at 14.5°C by 1°C is defined
as 1 calorie (cal), and 1 cal = 4.1868 J. The magnitudes of
the kilojoule and Btu are almost identical (1 Btu = 1.0551 kJ).
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DIMENSIONS AND UNITS
Dimensional homogeneity is a valuable tool in checking for errors. Make
sure every term in an equation has the same units.
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DIMENSIONS AND UNITS
Unity conversion ratios are helpful in converting units. Use them.
All nonprimary units ( secondary units ) can be formed by
combinations of primary units. Force units, for example, can be
expressed as
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DIMENSIONS AND UNITS
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PROPERTIES OF FLUID
Gases are light and compressible,
Liquids are heavy (by comparison) and relatively incompressible
Syrup flows slowly from a container than water
To quantify these differences certain fluid properties are used
Fluid properties include;
Mass (m) –already discussed!
Pressure – Already discussed!
Density ( ρ )
specific weight (w) specific gravity (sg )
Bulk modulus of elastisity (E)
viscosity i.e. Dynamic or kinematic viscosity
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PROPERTIES OF FLUID
Density, ρ (rho) of a fluid is defined as its mass (m) per unit
volume (V)
The value of ρ can vary widely between different fluids For liquids, variations in pressure and temperature generally
have only a small effect on the value of ρ
Unlike liquids, the density of a gas is strongly influenced by
both pressure and temperature
The maximum density ( ρ = 1000kg/m3 ) of water is reached at
40C
Specific volume, V s of fluid is its volume per unit mass
ρ = m/V (kg/m3 )
V s = V/m =1/ ρ (m3
/kg)
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PROPERTIES OF FLUID
Effect of temperature on the value of ρ of water
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PROPERTIES OF FLUID
Specific weight of a fluid, , (gamma), is defined as its weight perunit volume
The specific weight is related to density through the equation;
Specific gravity of a fluid, SG, is defined as the ratio of the densityof the fluid to the density of water at some specified temperature
Usually the specified temperature is taken as 40C (39.20F)and at thistemperature the density of water 1000kg/m3 or 1.94slug/ft3
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PROPERTIES OF FLUID
Density of Ideal Gases
Gases are highly compressible in comparison to liquid.
Changes in gas density directly related to changes in pressure
and temperature through the equation of ideal or perfect gas
law ;
The gas constant, R , depends on the particular gas and is
related to the molecular weight of the gas by equation;
R = R u /M R u , is universal gas constant
(8.314kJ/kmol K)
M , molecular weight
Where P , is absolute pressure (N/m2),
T , is are absolute temperature (K)
R , is gas constantP = ρRT
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PROPERTIES OF FLUID
Example 1:
A reservoir of oil has a mass of 825kg and a volume of
0.917m3 calculate;
Weight of the reservoir
The density, specific weight and specific gravity of the
oil
Example 2:
Glycerine at 20 0 C has a specific gravity of 1.263. compute its
density and specific weight . Example 3
A gas weighs 20N/m3 at 30 0 C and at an absolute pressure of
350kN/m2. Determine the gas constant and density of the
gas.
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BULK MODULUS OF ELASTICITY
The bulk modulus of elasticity or compressibility refer tothe change in volume (V) of a substance that is
subjected to a change in pressure on it.
Liquids are heavy and very slightly compressible
For liquids, very large change in pressure is required to
produce small change a in volume.
Gases light and compressible –bulk modulus is not
usually applied to gases.
For gases, to determine the change in volume of a gas
with a change in pressure, the principles of
thermodynamics must be applied
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VISCOSITY ( µ )
Different fluids deform at different rates when the sameshear stress (force/area) is applied.
Viscosity, µ is a fluid property that offers resistance to the
shear force or relative motion of fluid
It can be thought as the internal stickiness of a fluid
Representative of internal friction in fluids
Internal friction forces in flowing fluids result from cohesion
and momentum interchange between molecules.
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EFFECT OF TEMPERATURE ON VISCOSITY..
In liquids; viscosity decreases with increasing temperature
When temperature increases the distance between
molecules increases and the cohesive forcedecreases.
In gases;
The contribution to viscosity is more due to
momentum transfer
As temperature increases, more molecules cross over withhigher momentum differences and setting up strong internalshear
Thus, viscosity increases with increasing temperature
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Dynamic (absolute)
viscosity of some common
fluids as a function oftemperature
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MORE ON VISCOSITY...
Viscosity is important, for example,
In determining the amount of fluids that can be
transported in a pipeline during a specific period
of time
determining energy losses associated with
transport of fluids in ducts, channels and pipes
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NO SLIP CONDITION
Because of viscosity, at boundaries (walls) particles
of fluid adhere to the walls, and so the fluid velocity
is zero relative to the wall
Viscosity and associated shear stress may be
explained via the following: flow between no-slip
parallel plates.
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Flow between no-slip parallel plates-each plate has area A
Moving plate
Fixed plate
F U ,
Y
x z
y
F Fi
U Ui
Force induces velocity on top plate. At top plate flow velocity is
F
U
U
At bottom plate velocity is 0
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The velocity induced by moving top plate can be sketched as follows:
y
u y( )
Y
U
u yU
Y y( )
The velocity induced by top plate is expressed as:
u y( ) 0 0
u y Y U ( )
Slope: Take derivertive of the equation gives;The expression is valid
for most common fluids
such as water, gasoline
and airWhere: δβ is rate of shearing strain &
du/dy velocity gradient = slope
slope
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For a large class of fluids, empirically, F AU
Y
More specifically, F AU Y
; is coefficient of vis itycos
Shear stress induced by F is F
A
U
Y
From previous slide, note that
du
dy
U
Y
Thus, shear stress is du
dy
In general we may use this expression to find shear stress at a point
inside a moving fluid. Note that if fluid is at rest this stress is zero because
du
dy 0
F
A shear stress
x( )Recall: definition of Shear stress
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Alternatively: The shearing stress (τ) is directly propotional tothe rate of deformation/shearing strain(δβ)/velocity gradient
==>
The expression is know as Newton’s law of viscosity
Newton’s law of viscosity states that the shear force to beapplied for a deformation rate of (du/dy) over an area A isgiven by,
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du
dy
- Dynamic viscosity (coeff. of viscosity)
Fixed no-slip plate
u y velocity profile( ) ( )
Shear stress due to viscosity at a point:
fluid surface
e.g.: wind-driven flow in ocean
r - kinematic
viscosity
y
NEWTON’S EQUATION OF VISCOSITY
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N EWTONIAN AND NON -N EWTONIAN FLUIDS
Fluids for which the shearing stress is linearly related
to the rate of shearing strain are designated as
Newtonian fluids
Newtonian fluids obey eqn:
Fluids for which the shearing stress is not linearly
related to the rate of shearing strain are designated
as non-Newtonian fluids
Non-Newtonian fluids do not obey the above
equation
Linear variation of shearing stress with rate of shearing strain
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g g
for common fluids
V i ti f h i t ith t f h i t i f
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Variation of shearing stress with rate of shearing strain for
several types of fluids, including common non-Newtonian fluids
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SELF STUDY.....
Surface tension...
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END