chapter one fluid flow properties of fluid
TRANSCRIPT
Chapter one fluid flow properties of fluid
Qahtan A. Mahmood Page 1
Introduction
Fluid mechanics is a branch of physics concerned with the mechanics of fluids (liquids,
and gases,) and the forces on them. Fluid mechanics has a wide range of applications
Fluid mechanics can be divided into:
Fluid statics, the study of fluids at rest;
: مخل القح الت سلطب المبئع ف حبلخ السكن عل العبء الذ حت دراسخ المائع ف حبلخ السكن
Fluid kinematic is deal with fluid velocity type
:كبن تتم دراسخ سزعخ المبئع كفخ تغزب ثه وقطخ اخز كفخ تغز دراسخ المائع ف حبلخ الحزكخ
االوجة السزعخ مع الضغظ المسلظ ثه وقطته ف
Fluid dynamics, the study of the effect of forces on fluid motion,
دراسخ المبئع مه حج الق الت سلطب ف حبلخ الحزكخ
If a fluid affected by changes in pressure and temperature, it is said to be
Compressible fluid
مائع قبثلخ لالوضغبط حج تغز حجم المبئع ثتغز الضغظ درجخ الحزارح مخل الغبساد اثخزح الماد
Incompressible fluid,
السائل ف الحققخ المبئع الذ مائع قبثلخ لالوضغبط حج تغز حجم المبئع ثتغز الضغظ درجخ الحزارح مخل
مخل ذي الخبصخ ذع مبئع مخبل لس لذا المبئع جد,المبئع الحقق تغز حجم قلال ثتغز الضغظ درجخ
الحزارح كن عل وعه
Real fluid can be divided into:
Newtonian تجع قبون وته
Non Newtonian ال تجع قبون وته
Chapter one fluid flow properties of fluid
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1-1 Physical Properties of Fluids
1. DENSITY AND SPECIFIC GRAVITY
Density is defined as mass per unit volume [symbol: ρ (rho)]
Specific Volume [symbol: υ (upsilon)]
Is defined as the volume per unit mass, that is
Weight density or specific weight [symbol: (gamma).]
Is defined as weight per unit volume, that is,
Specific gravity or relative density[symbol: SG]
Is defined as the ratio of the density of a substance to the density of some
standard substance at a specified temperature (usually water at 4°C, for which H2O =
1000 kg/m3). That is,
Chapter one fluid flow properties of fluid
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2- Pressure
Pressure is the (compression) force exerted by a fluid per unit area.
(
)
The pressure developed at the bottom of a column of any liquid is called hydrostatic
pressure and is given by
3- Energy and specific heats
Potential energy is the work required to move the system of mass m from the
origin to a position against a gravity field g:
Kinetic energy is the work required to change the speed of the mass from zero to
velocity V.
In the analysis of systems that involve fluid flow, we frequently encounter the
combination of properties U and Pv. For convenience, this combination is called
enthalpy h. That is,
Chapter one fluid flow properties of fluid
Qahtan A. Mahmood Page 4
Where P/ is the flow energy, also called the flow work, which is the energy per unit
mass needed to move the fluid and maintain flow.
The internal energy U represents the microscopic energy of a non-flowing fluid per unit
mass,
Whereas enthalpy h represents the microscopic energy of a flowing fluid per unit mass
as shown in figure below
The total energy of a simple compressible, E of a substance is the sum of the internal,
kinetic, and potential energies on a unit-mass basis, it is expressed as (e = U + KE+ PE).
The fluid entering or leaving a control volume possesses an additional form of energy
the flow energy P/ . Then the total energy of a flowing fluid on a unit-mass basis
becomes
Where h = P/ + U is the enthalpy, u is the velocity, and z is the elevation of the system
relative to some external reference point
The differential and finite changes in the internal energy and enthalpy of an ideal gas
can be expressed in terms of the specific heats as
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For incompressible substances, the constant-volume and constant-pressure specific
heats are identical. Therefore, cp= cv= c for liquids, and the change in the internal
energy of liquids can be expressed as U = cave T.
Noting that constant for incompressible substances, the differentiation of
enthalpy h = U + P/ gives dh = dU + dP/ . Integrating, the enthalpy change becomes
h =U +P/ = cave T +P/
Therefore h =U = cave T for constant-pressure processes, and h =P/ for
constant-temperature processes of liquids.
4- The ideal gas equation of state
Any equation that relates the pressure, temperature, and density (or specific volume) of
a substance is called an equation of state. The simplest and best-known equation of
state for substances in the gas phase is the ideal-gas equation of state, expressed as
Where: Ru is the gas universal constant, Ru = 8.314 (kJ/kmol .K). The ideal gas
equation can be written as follows:
The constant R is different for each gas; for air, Rair = 0.287 kJ/kg.K. The molecular
weight of air M=28.97 kg/kmol.
5- Dynamic viscosity [symbol: μ (mu)]
The viscosity of a fluid is a measure of its resistance to shear or angular deformation.
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6- Kinematic viscosity [symbol: ν (nu)]
It is the ratio of the dynamic viscosity to mass density of fluid,
7. Surface tension [symbol: σ (sigma)]
The surface of a liquid is apt to shrink, and its free surface is in such a state where each
section pulls another as if an elastic film is being stretched. The tensile strength per unit
length of assumed section on the free surface is called the surface tension. Liquid
droplets behave like small spherical.
The pulling force that causes this tension acts parallel to the surface and is due to the
attractive forces between the molecules of the liquid. The magnitude of this force per
unit length is called surface tension σ s and is usually expressed in the unit N/m (or
lbf/ft in English units).
Let d as the diameter of the liquid drop, σ as the surface tension, and p as the increasing
in internal pressure.
التتز السطح ظبزح فشبئخ تحذث إحز جد قح تمبسك ثه جشئبد المبدح السبئلخ، حج تعط السائل
صفخ األغشخ المتمبسكخ، تحذث إحز تعزض الجشئبد المجدح داخل السبئل لق الشذ مه كل االتجببد، فتلغ
تتأحز ثبلق المجدح ف األسفل الجاوت، ممب كل مىمب األخز، أمب الجشئبد المجدح عل سطح السبئل ف
جعل السطح مشذدا لألسفل؛ فظز عل ئخ غشبء.
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Qahtan A. Mahmood Page 7
1-2 the flow rate
Volumetric flow rate [symbol: Q]
It is the volume of fluid transferred per unit time.
Where: A is the cross sectional area of flow normal to the flow direction.
Mass flow rate [symbol: m]
It is the mass of fluid transferred per unit time.
Mass flux or (mass velocity) [symbol: G]
It is the mass flow rate per unit area of flow,
1-3 Newton’s Law of Viscosity and Momentum Transfer
Consider a fluid layer between two very large parallel plates separated by a distance L
as shown in figure (1-1). Now a constant parallel force (F) is applied to the upper plate
while the lower plate is held fixed. The fluid in contact with the upper plate sticks to the
plate surface and moves with it at the same velocity, and the shear stress ( ) acting on
this fluid layer is
Where: A is the contact area between the plate and the fluid.
y is the vertical distance from the lower plate.
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Figure (1-1) The behavior of a fluid in laminar flow between two parallel plates
In steady laminar flow, the fluid velocity between the plates varies linearly
between 0 and V, and thus the velocity profile and the velocity gradient are
The velocity gradient is directly proportional to the shear stress
Fluids for which the rate of deformation is proportional to the shear stress are called
Newtonian fluids.
Most common fluids such as water, air, gasoline, and oils are Newtonian fluids. Blood
and liquid plastics are examples of non-Newtonian fluids
In one-dimensional shear flow of Newtonian fluids, shear stress can be expressed by the
linear relationship
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A plot of shear stress versus the rate of
deformation (velocity gradient) for a
Newtonian fluid is a straight line whose
slope is the viscosity of the fluid, as shown
in Figure (1-2). Note: that viscosity is
independent of the rate of deformation
figure (1-2): The rate of deformation (velocity gradient)
The shear force acting on a Newtonian fluid layer (or, by Newton’s third law, the force
acting on the plate) is
The viscosity of liquids decreases with temperature, whereas the viscosity of gases
increases with temperature
This is because in a liquid the molecules possess more energy at higher temperatures,
and they can oppose the large cohesive intermolecular forces more strongly. As a result,
the energized liquid molecules can move more freely.
In a gas, on the other hand, the
intermolecular forces are negligible,
and the gas molecules at high
temperatures move randomly at
higher velocities. This results in
more molecular collisions per unit
volume per unit time and therefore
result greater resistance to flow.
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Consider a fluid layer of thickness L within a small gap between two concentric
cylinders, as shown in figure (1-3) below such as the thin layer of oil in a journal
bearing.
Figure (1-3): Cylindrical moving
The gap between the cylinders can be modeled as two parallel flat plates separated by a
fluid.
the wetted surface area of the inner cylinder to be A = 2RL
torque can be expressed as
Where L is the length of the cylinder and n is the number of revolutions per unit time,
Equatio1-3 can be used to calculate the viscosity of a fluid by measuring torque at a
specified angular velocity. Therefore, two concentric cylinders can be used as a
viscometer, a device that measures viscosity.
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1-4 Newtonian and non-Newtonian fluids
Plot the relationship between shear stress and rate of deformation as shown in Figure
(1-4). The slope of the curve on the () versus du/dy chart is referred to as the apparent
viscosity of the fluid.
For Newtonian fluids, the relationship between shear stress and rate of
deformation is linear.
For non-Newtonian fluids, the relationship between shear stress and rate of
deformation is not linear, and are divided into
a) Fluids for which the apparent viscosity increases with the rate of deformation
(such as solutions with suspended starch or sand) are referred to as dilatant .
b) The fluid becoming less viscous as it is sheared harder ( such as some paints,
polymer solutions, and fluids with suspended particles) are referred to as
pseudoplastic or shear thinning fluids.
c) Some materials such as toothpaste can resist a finite shear stress and thus behave
as a solid, but deform continuously when the shear stress exceeds the yield stress
and thus behave as a fluid. Such materials are referred to as Bingham plastics
Figure (1-4): Plot the relationship between shear stress and rate of deformation
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Example (1.1)
One liter of certain oil weighs 0.8 kg calculates the specific weight, density, specific
volume, and specific gravity of it.
Solution:
Specific weight
Density
Specific volume
Specific gravity
Example (1.2)
Determine the specific gravity of a fluid having viscosity of (4.0 c.poise ) and kinematic
viscosity of (3.6 c.stoke)
Solution
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Example (1.3)
A flat plate of area 2x104 cm
2 is pulled with a speed of 0.5 m/s relative to another plate
located at a distance of 0.2 mm from it. If the fluid separated the two plates has a
viscosity of (1.0 poise), find the force required to maintain the speed.
Solution
Example (1.4)
A shaft of diameter 10 cm having a clearance of 1.5 mm rotates at 180 rpm in a bearing
which is lubricated by an oil of viscosity 100 c.p. Find the intensity of shear of the
lubricating oil if the length of the bearing is 20 cm and find the torque.
Solution:
The linear velocity of rotating is
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The torque is equivalent to rotating moment
T=FR =F (D/2) =3.95N*(0.1/2)m=0.1975J
Example (1.5)
A plate of size 60 cm x 60 cm slides over a plane inclined to the horizontal at an angle
of 30°. It is separated from the plane with a film of oil of thickness 1.5 mm. The plate
weighs 25kg and slides down with a velocity of 0.25 m/s. Calculate the dynamic
viscosity of oil used as lubricant. What would be its kinematic viscosity if the specific
gravity of oil is( 0.95)
Solution:
Component of W along the plane =W cos(60) =W sin(30)
= 25 (0.5) = 12.5 kg
F = 12.5 kg (9.81 m/s2) =122.625 N
τ = F/A = 122.625 N/(0.6 x0.6) m2 = 340.625 Pa