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Module-1-Part-1

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M
FLUID
ECHANICS
FLUID
PROPERTIES
Module 1
FLUID PROPERTIES
Module 1
Density and Specific Weight
Viscosity
Compressibility
Surface Tension
Capillary Action
Vapor Pressure
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FLUID
ECHANICS
Density and Specific Weight
Density is defined as mass per unit volume.
𝝆=
π’Ž
𝑽
The density for air at standard atmospheric conditions,
that is, at a pressure of 101.3 kPa and a temperature of
15°C, is 1.23 kg/m3. For water, the nominal value of density
is 1000 kg/m3.
Specific gravity is the ratio of the density of a substance to
the density of water at a reference temperature of 4°C.
𝑺=
π†π’˜π’‚π’•π’†π’“
𝑾 π’Žπ’ˆ
=
= π†π’ˆ
𝑽
𝑽
π†π’˜π’‚π’•π’†π’“
=
𝜸
πœΈπ’˜π’‚π’•π’†π’“
The density and specific weight of water do vary slightly
with temperature, as described below:
Specific weight is defined as weight per unit volume.
𝜸=
𝝆
𝑻−πŸ’
= 𝟏𝟎𝟎𝟎 −
πŸπŸ–πŸŽ
𝟐
where g is the local gravity. The units of specific weight are
N/m3. For water, the nominal value is 9800 N/m3.
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FLUID
ECHANICS
Density and Specific Weight (Sample Problem 1)
A reservoir of glycerin has a mass of 1200 kg and a volume of 0.952 m3. Find the glycerin’s weight (π‘Š), mass density
(𝜌), specific weight (𝛾), and specific gravity (𝑠. 𝑔.).
Solution
π‘Š = π‘šπ‘” = 1200 π‘˜π‘” 9.81 π‘šπ‘  2 = πŸπŸπŸ•πŸ•πŸŽ 𝑡 𝒐𝒓 𝟏𝟏. πŸ•πŸ• π’Œπ‘΅
𝜌=
π‘š 1200 π‘˜π‘”
=
= πŸπŸπŸ”πŸ π’Œπ’ˆ/π’ŽπŸ‘
3
𝑉 0.952 π‘š
𝛾=
π‘Š 11.77 π‘˜π‘
=
= 𝟏𝟐. πŸ‘πŸ” π’Œπ‘΅/π’ŽπŸ‘
3
𝑉
0.952 π‘š
𝑠. 𝑔. =
𝛾
𝛾𝐻2𝑂
=
12.36
= 𝟏. πŸπŸ”
9.81
M
FLUID
ECHANICS
Density and Specific Weight (Sample Problem 2)
Estimate the density of water at 80°C.
Solution
The variation of density of water with temperature is given by:
𝟐
π†π’˜π’‚π’•π’†π’“
𝑻−πŸ’
= 𝟏𝟎𝟎𝟎 −
πŸπŸ–πŸŽ
2
πœŒπ‘€π‘Žπ‘‘π‘’π‘Ÿ
80 − 4
= 1000 −
180
πœŒπ‘€π‘Žπ‘‘π‘’π‘Ÿ = 968 π‘˜π‘”/π‘š3
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FLUID
ECHANICS
Viscosity
Lesson 1.2
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FLUID
ECHANICS
Viscosity
Viscosity is a measure of a fluids resistance to flow, or the
stickiness of a fluid. Consider Fig. 1 in which the fluid
particles move in the x-direction at different speeds, so that
particle velocities 𝒖 vary with the y-coordinate 𝒖 = 𝒖 π’š .
𝑡
π’ŽπŸ
𝑡−𝒔
π’ŽπŸ
where 𝝉 − shear stress
𝝁 − viscosity
Figure 1. Shear stress in fluid.
We can define the viscosity 𝝁 of the fluid by the relationship:
𝝉=𝝁
𝒅𝒖
π’…π’š
𝒅𝒖
− velocity gradient or strain rate
π’…π’š
The concept of viscosity can also be illustrated by
considering a fluid within the small gap between two
concentric cylinders.
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FLUID
ECHANICS
Viscosity
a) the two cylinders; b) rotating inner cylinder; c) velocity
distribution; d) the inner cylinder. The outer cylinder is fixed and
the inner cylinder is rotating.
The only stress that exists to resist the applied torque for
this simple flow is a shear stress, which is observed to
depend directly on the velocity gradient; that is;
𝝉=𝝁
𝒅𝒖
𝒅𝒓
where:
𝒖 − tangential velocity component
which depends only on π‘Ÿ
𝒅𝒖
− velocity gradient
π’…π’š
For a small gap (β„Ž β‰ͺ 𝑅 ) this gradient can be approximated
by using a linear velocity distribution in the gap.
Figure 2. Shear stress in fluid between two concentric cylinders.
M
FLUID
ECHANICS
Viscosity
Thus,
𝒅𝒖 πŽπ‘Ή
=
𝒅𝒓
𝒉
where:
𝒉 − is the gap width.
Thus, we can relate the applied torque 𝑇 to the viscosity
and other parameters by the equation
𝑻 = π‘ π‘‘π‘Ÿπ‘’π‘ π‘  π‘₯ π‘Žπ‘Ÿπ‘’π‘Ž π‘₯ π‘šπ‘œπ‘šπ‘’π‘›π‘‘ π‘Žπ‘Ÿπ‘š
𝑻 = 𝝉 𝒙 πŸπ…π‘Ήπ‘³ 𝒙 𝑹
𝑻=𝝁
πŽπ‘Ή
𝒙 πŸπ…π‘Ήπ‘³ 𝒙 𝑹
𝒉
πŸπ…π‘ΉπŸ‘ πŽπ‘³π
𝑻=
𝒉
𝑳 − represents the length of the rotating cylinder.
Figure 2. Shear stress in fluid between two concentric cylinders.
M
FLUID
ECHANICS
Viscosity
Newtonian Fluids – fluids with constant viscosity no matter the amount of shear applied for a constant temperature. The
shear rate is directly proportional to shear stress.
Figure 3. Velocity profile of a Newtonian fluid.
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FLUID
ECHANICS
Viscosity
Non-newtonian fluid has viscosity which does not vary linearly with shear stress; viscosity can change when under stress to
either more liquid or more solid.
Pseudoplastics become less resistant to motion with increased strain rate.
(b)
(c)
(a)
Figure 4. Pseudoplastics: (a) Honey, (b) Paint, (c) Catsup.
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FLUID
ECHANICS
Viscosity
Dilatants (quicksand, slurries) become more resistant to motion as the strain rate increases.
(a)
(b)
Figure 5. Dilatants: (a) Liquid armor, (b) Walking on top of a dilatant.
M
FLUID
ECHANICS
Viscosity
Ideal plastics (or Bingham fluids) require a minimum shear stress to cause motion.
(a)
(b)
Figure 6. Bingham fluids: (a) Toothpaste, (b) Mayonnaise.
M
FLUID
ECHANICS
Viscosity
Figure 7. Classification of fluids according to viscosity.
M
FLUID
ECHANICS
Viscosity
Since the viscosity is often divided by the density in the derivation of equations, it has become useful and
customary to define kinematic viscosity to be
𝒗=
𝝁
𝝆
where:
𝒗 − is in π’ŽπŸ /𝒔
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FLUID
ECHANICS
Viscosity (Sample Problem 1)
Rearranging Eq. 3
A viscometer is constructed with two 30-cm-long
concentric cylinders, one 20.0 cm in diameter and the
other 20.2 cm in diameter. A torque of 0.13 N-m is
required to rotate the inner cylinder at 400 rpm
(revolutions per minute). Calculate the viscosity.
Solution
𝝁=
=
𝑻𝒉
πŸπ…π‘ΉπŸ‘ πŽπ‘³
0.13(0.001)
2πœ‹ 0.1 3 (41.89)(0.3)
= 𝟎. πŸŽπŸŽπŸπŸ”πŸ’πŸ” 𝑡 − 𝒔/π’ŽπŸ
The applied torque is just balanced by a resisting torque
due to the shear stresses.
Given
𝐿 = 30 π‘π‘š = 0.3 π‘š
𝑑1 = 20.0 π‘π‘š = 0.2 π‘š
𝑑2 = 20.2 π‘π‘š = 0.202 π‘š
𝑇 = 0.13 𝑁 − π‘š
𝑑
= 10 π‘π‘š
2
2πœ‹
πœ” = 400 π‘₯
= 41.89 π‘Ÿπ‘Žπ‘‘/𝑠
60
𝑅=
β„Ž = (𝑑2 −𝑑1 )/2 = 0.1 π‘π‘š
𝑁 = 400 π‘Ÿπ‘π‘š
M
FLUID
ECHANICS
Viscosity (Sample Problem 2)
The velocity distribution in a 4-cm-diameter pipe transporting
20°C of water is given by 𝑒 π‘Ÿ = 10(1 − 2500π‘Ÿ 2 ) m/s. Calculate
the shearing stress at the wall. Viscosity of water at 20°C is 10-3
N.s/m2.
Solution
The shear stress is given by:
𝜏=πœ‡
𝑑𝑒
π‘‘π‘Ÿ
We determine du/dr from the given expression for u as:
𝑑𝑒
𝑑
=
10(1 − 2500π‘Ÿ 2 ) = −50,000π‘Ÿ
π‘‘π‘Ÿ π‘‘π‘Ÿ
At the wall r = 2 cm = 0.02 m. Substituting r in the above equation:
𝑑𝑒
= 50,000π‘Ÿ = 1000/𝑠
π‘‘π‘Ÿ
Substitute in the equation for shear stress to get
𝜏=πœ‡
𝑑𝑒
𝑁. 𝑠 1000
𝑁
= 10−3 2 π‘₯
= 1 2 = 𝟏 𝑷𝒂 (𝑨𝒏𝒔. )
π‘‘π‘Ÿ
π‘š
𝑠
π‘š
M
FLUID
ECHANICS
Viscosity (Sample Problem 3)
Consider a fluid flow between two parallel fixed plates 5 cm apart
as shown. The velocity distribution for the flow is given by 𝑒 𝑦 =
120 0.05𝑦 − 𝑦 2 m/s where 𝑦 is in meters. The fluid is water at
10°C. Calculate the magnitude of the shear stress acting on each
of the plates. At 10°C, πœ‡ = 1.308 π‘₯ 10−3 𝑁. 𝑠/π‘š2 .
Solution
𝜏=πœ‡
The shear stress is given by:
𝑑𝑒
𝑑
=
120 0.05𝑦 − 𝑦 2
𝑑𝑦 𝑑𝑦
𝑑𝑒
𝑑𝑦
= 120 0.05 − 2𝑦
At the lower plate where y = 0:
𝜏=πœ‡
𝑑𝑒
= 1.308 π‘₯ 10−3 π‘₯ 120(0.05 − 2 0 )
𝑑𝑦
π‰π’š=𝟎 = πŸ•. πŸ–πŸ’πŸ– 𝒙 𝟏𝟎−πŸ‘
𝑡
π’ŽπŸ
(𝑨𝒏𝒔. )
At the upper plate where 𝑦 = 0.05 π‘š:
𝜏=πœ‡
𝑑𝑒
= 1.308 π‘₯ 10−3 π‘₯ 120(0.05 − 2 0.05 )
𝑑𝑦
π‰π’š=𝟎 = πŸ•. πŸ–πŸ’πŸ– 𝒙 𝟏𝟎−πŸ‘
𝑡
π’ŽπŸ
(𝑨𝒏𝒔. )
M
FLUID
ECHANICS
Compressibility
All fluids compress if the pressure increases, resulting in
a decrease in volume or an increase in density. A
common way to describe the compressibility of a fluid is
by bulk modulus of elasticity B.
Bulk modulus of elasticity, also called coefficient of
compressibility is defined as the ratio of the change in
pressure to the relative change in density or volume while
the temperature remains constant. It has the same units
as pressure.
𝑩=
βˆ†π’‘
βˆ†π’‘
=
βˆ†π†/𝝆 βˆ†π‘½/𝑽
The bulk modulus for water at standard conditions is
approximately 2100 MPa. To cause 1% change in the
density of water a pressure of 21 MPa (210 atm) is
required.
The bulk modulus can also be used to calculate the
speed of sound in a liquid;
𝒄=
𝜷
𝝆
This yields approximately 1450 m/s for the speed of
sound in water at standard conditions.
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FLUID
ECHANICS
Compressibility (Sample Problem 1)
Two engineers wish to estimate the distance across a
lake. One pounds two rocks together under water on one
side of the lake and the other submerges his head and
hears a small sound 0.62 s later, as indicated by a very
accurate stopwatch. What is the distance between the
two engineers?
Solving for the speed of sound c:
𝑐=
211 π‘₯ 10−7
= 1453 π‘š/𝑠
999.7
The distance across the lake is,
Solution
The sound will travel across the lake at the speed of
sound in water. The speed of sound in water is calculated
using:
𝑐=
𝐿 = π‘βˆ†π‘‘ = 1453 π‘₯ 0.62 = πŸ—πŸŽπŸ π’Ž
(𝑨𝒏𝒔. )
𝛽
𝜌
Assuming the temperature of the lake is 10°C
Bulk modulus of elasticity 𝛽 = 211 π‘₯ 10−7 π‘ƒπ‘Ž
Density ρ = 999.7 π‘˜π‘”/π‘š3
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FLUID
ECHANICS
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