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Lecture 2 Fluid Statics 2024

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03/03/2024
CIV1202 FLUID MECHANICS
Unit 2: Hydrostatics
Eng. Dr. Seith Mugume (PhD, MUIPE, REng)
Lecturer, Department of Civil and Environmental Engineering
College of Engineering, Design, Art and Technology
Makerere University
Email: seith.mugume@mak.ac.ug; smugume@gmail.com
Tel: +256 771 358 124
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Course Content
Unit 2: Hydrostatics
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Pressure in fluids
• Pressure, p, is defined as force per unit area:
๐น๐‘œ๐‘Ÿ๐‘๐‘’
๐น
• p = ๐ด๐‘Ÿ๐‘’๐‘Ž = ๐ด [Units – Nm-2 or Pa]
• Atmospheric pressure (1 atm.) is equal to
101,325 Nm-2.
The
fluid
exerts
pressure
internally as well as on the same
container. The internal pressure is
the same in all directions
Unit 2: Hydrostatics
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Pressure in fluids
• In the presence of gravity, pressure
in a static fluid increases with
depth. This allows an upward
pressure force to balance the
downward gravitational force.
• This condition is hydrostatic
equilibrium.
• Incompressible fluids like liquids
have constant density; for them,
pressure as a function of depth h is
p = p0 + ρgh
where p0 = pressure Unit
at2:surface
Hydrostatics
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Pressure & Head
Vertical pressure relationship:
๐‘‘๐‘
= −๐œŒ๐‘”
๐‘‘๐‘ง
Integrating gives:
๐‘ = −๐œŒ๐‘”๐‘ง + ๐‘๐‘œ๐‘›๐‘ ๐‘ก๐‘Ž๐‘›๐‘ก
If z is measured from the free surface,
๐‘ง = −โ„Ž
๏ƒž ๐‘ = ๐œŒ๐‘”โ„Ž + ๐‘๐‘œ๐‘›๐‘ ๐‘ก๐‘Ž๐‘›๐‘ก
๏ƒž The surface pressure is the atmospheric pressure, ๐‘๐‘Ž๐‘ก๐‘š
๏ƒž ๐‘๐‘Ž๐‘ก๐‘š = constant
๏ƒž ๐‘ = ๐œŒ๐‘”โ„Ž + ๐‘ƒ๐‘Ž๐‘ก๐‘š
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Pressure and head
• It is often convenient to take atmospheric pressure
as the datum. Pressure quoted this way is known as
gauge pressure
๐‘ƒ๐‘”๐‘ข๐‘Ž๐‘”๐‘’ = ๐œŒ๐‘”โ„Ž
• Lower limit of any pressure is the pressure
measured in perfect vacuum
• Pressure measured above a perfect vacuum (zero)
is known as absolute pressure
๐‘ƒ๐‘Ž๐‘๐‘ ๐‘œ๐‘™๐‘ข๐‘ก๐‘’ = ๐œŒ๐‘”โ„Ž + ๐‘ƒ๐‘Ž๐‘ก๐‘š
=> Absolute pressure = (Gauge + Atmospheric)
pressure
Unit 2: Hydrostatics
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Gauge Pressure, p
• Gauge pressure can be given using the height of
any fluid.
๐‘ = ๐œŒ๐‘”โ„Ž
• Vertical height, h corresponds to the head
• If pressure is quoted as head, then the density of
the fluid should be specified
Example:
What is pressure of 500 kN/m2 in terms of head of:
a)
b)
c)
Water of density, ๐œŒ = 1,000 kg/m3
Mercury of density, ๐œŒ = 13.6 x 103 kg/m3
A fluid with relative density, ๐›พ = 8.7
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Pressure measurement
• Manometers
– Single tube
– U-tube
• Piezometers
• Bourdon gauges
Unit 2: Hydrostatics
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Pressure measurement
• A manometer is applied to measure
pressure differences.
• Manometers use the relationship between
pressure head to measure pressure.
• Gauge pressure is a measure of pressure
relative to the ambient atmosphere:
p = patm + ρgh
=> Manometer measures gauge pressure
Unit 2: Hydrostatics
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Piezometric tube manometer
• Simplest manometer is an
open tube
• Attached to the top of the
container containing liquid at
pressure
• Tube open to atmosphere
• Measured pressure is relative
to atmospheric pressure =>
Gauge pressure
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Piezometric tube manometer
• Pressure at A, PA
๐‘ƒ๐ด = ๐œŒ๐‘”โ„Ž1
• Pressure at B, PB
๐‘ƒ๐ต = ๐œŒ๐‘”โ„Ž2
Problems with Piezometers
a) Can only be used for liquids
b) Pressure must be above atmospheric
c) Liquid height must not be too small or too
large
Unit 2: Hydrostatics
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Pressure measurement
Unit 2: Hydrostatics
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Exercise 2
What is the maximum gauge pressure of
water that can be measured by a piezometer
of height 1.5m? And if the liquid had a
relative density of 8.5, what would be the
maximum gauge pressure?
Solution:
a) Water
๐‘ƒ๐‘”๐‘Ž๐‘ข๐‘”๐‘’ = ๐œŒ๐‘”โ„Ž = 1000 x 9.81 x 1.5 = 14,715 N/m2 (14.715 kN/m2)
b) Liquid with relative density of 8.5
๐‘ƒ๐‘”๐‘Ž๐‘ข๐‘”๐‘’ = ๐œŒ๐‘”โ„Ž = 8.5 x 1000 x 9.81 x 1.5 = 125,077.5 N/m2
(125.077 kN/m2)
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Equality of pressure
• Consider a horizontal cylindrical element
• Cross sectional area = A; Mass density = ๐œŒ; Left end pressure
= pl; Right end pressure = pr
• For equilibrium, the sum of forces in the x direction is zero
• ๐’‘๐’ ๐‘จ = ๐’‘๐’“ ๐‘จ ⇒ ๐’‘๐’ = ๐’‘๐’“ (Horizontal direction ๏ƒณ Constant
pressure)
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The “U”-Tube Manometer
•
Enables the pressure of both liquids and gases to be measured
•
“U” tube is connected as shown and filled with the manometric fluid
•
Manometric fluid density should be greater than density of the fluid
being measured ๐œŒ๐‘š๐‘Ž๐‘› > ๐œŒ
•
The two fluids should not be able to mix ๏ƒณ immiscible
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The “U”-tube Manometer
• Pressure in a continuous static fluid is the
same at any horizontal level
• Pressure at B, pB = Pressure at C, pC
• For the left arm;
pB = pA+ pressure of height of liquid measured
๐‘๐ต = ๐‘๐ด + ๐œŒ๐‘”โ„Ž1
• For the right arm;
๐‘๐ถ = ๐‘๐‘Ž๐‘ก๐‘š + ๐œŒ๐‘š๐‘Ž๐‘› ๐‘”โ„Ž2 (omit patm)
๐‘๐ต = ๐‘๐ถ => ๐‘๐ด + ๐œŒ๐‘”โ„Ž1 = ๐œŒ๐‘š๐‘Ž๐‘› ๐‘”โ„Ž2
=> ๐’‘๐‘จ = ๐†๐’Ž๐’‚๐’ ๐’ˆ๐’‰๐Ÿ − ๐†๐’ˆ๐’‰๐Ÿ
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Gas pressure measurement
• The manometer works in the same way for
gases
• However, the manometric fluid is liquid
(i.e. mercury, oil or water)
• Liquid density is much greater than gas
=> ๐œŒ๐‘š๐‘Ž๐‘› โ‰ซ ๐œŒ
๐œŒ๐‘”โ„Ž1 can be neglected
Gauge pressure = ๐†๐’Ž๐’‚๐’ ๐’ˆ๐’‰๐Ÿ
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Exercise 3
Using a “U”-tube manometer to measure
gauge pressure of fluid density ๐œŒ =
700 ๐‘˜๐‘”/๐‘š3 , and the manometric fluid is
mercury, with relatively density of 13.6. What
is the gauge pressure if:
a) h1 = 0.4 m and h2 = 0.9 m ?
b) h1 = 0.4 m and h2 = -0.1 m ?
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Pressure difference
measurement using a “U”-tube
manometer
๐‘๐ถ = ๐‘๐ท
๐‘๐ถ = ๐‘๐ด + ๐œŒ๐‘”โ„Ž๐‘Ž
๐‘๐ท = ๐‘๐ต + ๐œŒ๐‘” โ„Ž๐‘ − โ„Ž + ๐œŒ๐‘š๐‘Ž๐‘› ๐‘”โ„Ž
๐‘๐ด − ๐‘๐ต
= ๐‘๐‘ − ๐œŒ๐‘”โ„Ž๐ด − ๐‘๐ท + ๐œŒ๐‘” โ„Ž๐ต − โ„Ž
+ ๐œŒ๐‘š๐‘Ž๐‘› ๐‘”โ„Ž
= ๐†๐’ˆ ๐’‰๐‘ฉ − ๐’‰๐‘จ + (๐†๐’Ž๐’‚๐’ − ๐†)๐’ˆ๐’‰
For gases,
๐œŒ๐‘š๐‘Ž๐‘› โ‰ซ ๐œŒ
๐’‘๐‘จ − ๐’‘๐‘ฉ = ๐†๐’Ž๐’‚๐’ ๐’ˆ๐’‰
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Pressure forces on submerged
bodies
Key static fluid principles already introduced
• Hydrostatic vertical pressure distribution
๐‘‘๐‘
= −๐œŒ๐‘”
๐‘‘๐‘ง
• Pressure at any equal depths in a continuous fluid
are equal
• In an uninterrupted fluid continuum, pressure at
any point acts equally in all directions (Pascal’s
law)
• Forces from a fluid on a boundary act at right
angles to that boundary
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Pressure on plane surfaces
• Consider a solid object
submerged in a liquid
– Liquid applies a pressure force
which is perpendicular to the
surface of the object at all
points
– All other pressure components
are also in equilibrium (unless
if there is relative motion
between the liquid and the
object)
Pressure at a point in a liquid
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Pressure on plane surfaces
Pressure force on a plate (a) Horizontal plate (b) Vertical plate
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(a) Horizontal plate
• Consider a flat plate with width, B, length,
L, suspended in water horizontally at
depth y.
⇒ ๐‘ = ๐œŒ๐‘”๐‘ฆ
โ–ช For y = 2 m, B = 1m, and L = 2.5 m; Calculate
the pressure at depth of 2 m
โ–ช Calculate the total force, F on the top surface
of the plate
Solution (p = 19,620 N/m2; F = 49,050 N)
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(a) Horizontal plate
• In most cases, engineers find it more
convenient to treat the total (or resultant)
force as if it was concentrated at a point
(as opposed to a distributed load)
• Point => Centre of Pressure or Point of
action
• The resultant force will act through the
centre of pressure, acting a right angles
to the plane through the centre of pressure
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(b) Vertical plate
• Pressure, p increases with depth
• At the water surface, gauge pressure = 0
• At the bottom of the plate, pressure, ๐‘ = ๐œŒ๐‘”๐‘ฆ =
1,000 × 9.81 × 2.5 = 24,525 ๐‘
• For linear pressure variation with y,
F = Average pressure x Area
24,525
๐น=
× 1 × 2.5 = 30,656 ๐‘
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Note: Locating the point of action of F is not so easy
as for the horizontal plate problem. A more general
approach is needed
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(b) Vertical plate
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(b) Vertical plate
• Consider a small element ๐›ฟ๐ด. The force, ๐›ฟ๐น acting on that
area due to pressure of the liquid, is ๐‘๐›ฟ๐ด.
– ๐‘ is not constant
– For an element at a distance, y below the free surface of the
liquid;
๐‘ = ๐œŒ๐‘”๐‘ฆ
๐›ฟ๐น = ๐œŒ๐‘”๐‘ฆ๐›ฟ๐ด
Therefore, the total force, ๐น = ๐œŒ๐‘” โ€ซ๐ด๐›ฟ๐‘ฆ ืฌโ€ฌ
For ๐‘ฆ = ๐‘™๐‘ ๐‘–๐‘›๐œƒ;
๐น = ๐œŒ๐‘” เถฑ ๐‘™๐‘ ๐‘–๐‘›๐œƒ๐›ฟ๐ด = ๐œŒ๐‘”(๐‘ ๐‘–๐‘›๐œƒ) เถฑ ๐‘™๐‘‘๐ด
โ€ซ >= ๐ด๐‘‘๐‘™ ืฌโ€ฌgeometric characteristic of the shape: First moment of
Area
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(b) Vertical plate
• โ€ซ = ๐ด๐‘‘๐‘™ ืฌโ€ฌproduct of ๐ด๐‘™ าง
Where A is the area of the plane surface and ๐‘™ าง is the distance from the
origin O to the centroid of the plane.
๏ƒž ๐น = ๐œŒ๐‘” ๐‘ ๐‘–๐‘›๐œƒ ๐ด๐‘™ าง
• In addition to the magnitude of the force, F, it is also necessary to the
precise location and angle of its line of action
•
– Pressure is distributed over the whole immersed body
– Nonetheless, a concentrated point load is considered
– ๐›ฟ๐น produces a moment ๐›ฟ๐น๐‘™ about the origin
– ๐‘š๐‘œ๐‘š๐‘’๐‘›๐‘ก = ๐›ฟ๐น๐‘™ = ๐œŒ๐‘”๐‘ฆ๐›ฟ๐ด๐‘™ = ๐œŒ๐‘”๐‘™ ๐‘ ๐‘–๐‘›๐œƒ ๐›ฟ๐ด๐‘™ = ๐œŒ๐‘” ๐‘ ๐‘–๐‘›๐œƒ ๐‘™2 ๐›ฟ๐ด
In the limit, ๐‘‘๐น๐‘™ = ๐œŒ๐‘” ๐‘ ๐‘–๐‘›๐œƒ ๐‘™ 2 ๐‘‘๐ด
•
Considering the whole surface,
๐‘š๐‘œ๐‘š๐‘’๐‘›๐‘ก = ๐น๐‘™ = ๐œŒ๐‘” ๐‘ ๐‘–๐‘›๐œƒ เถฑ ๐‘™2 ๐‘‘๐ด
Quantity โ€ซ ๐‘™ ืฌโ€ฌ2 ๐‘‘๐ด is another geometric characteristic => Second moment of area, I
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• Distance from the origin to the point of action,
• ๐‘™′ =
๐‘š๐‘œ๐‘š๐‘’๐‘›๐‘ก
๐œŒ๐‘” ๐‘ ๐‘–๐‘›๐œƒ ๐ผ
๐ผ
=
= าง
๐‘“๐‘œ๐‘Ÿ๐‘๐‘’
๐œŒ๐‘” ๐‘ ๐‘–๐‘›๐œƒ ๐ด๐‘™ าง
๐ด๐‘™
• I is evaluated using the Parallel axes theorem
๐ผ = ๐ผ๐‘œ + ๐ด๐‘™ 2าง
Where:
o I is the second moment of area of a plane surface about
origin O
o Io is the second moment of area of the surface about an
axis through its centroid
The axis is parallel to the axis at O. Io is a function of
geometric shape. ๐ด๐‘™ 2าง is the proportion of I due to the
distance from O to the centroid of the surface.
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2nd Moment of Area about a line through
the centroid of some common shapes
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Exercise
A rock fill dam is designed to have a cross section as represented in the figure
below. The reservoir design depth is to be 10 m. Estimate
(a) The forces on the dam per unit width
(b) The location of the centre of pressure
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Pressure forces on Curved
Surfaces
• Not all immersed
structures are flat
• Some dams have an
upstream face that may
be curved in both
vertical and horizontal
directions
• Other types of hydraulic
control structures such
as gates may also be
curved
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Pressure forces on curved
surfaces
• Pressure force is acts perpendicular to the immersed
surface
• Pressure on a curved surface is unevenly distributed
• The force is resolved into horizontal (๐›ฟ๐น๐‘ฅ ) and vertical
(๐›ฟ๐น๐‘ฆ )components
• ๐›ฟ๐น๐‘ฆ = total weight of the volume of the fluid above the
surface => Acts through the centre of gravity
• ๐›ฟ๐น๐‘ฅ = pressure force on vertical plane surface equal in
height to the projected height of the curved surface =>
Acts at distance ๐‘™′ below the free surface of the fluid
• Resultant force acts through the point of intersection of
lines of action W and Fx
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Pressure forces on curved
surfaces
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Exercise 1: Hydrostatic Force on
a Quadrant gate
Determine the magnitude and direction of
the resultant force of water on the quadrant
gate below. The principal dimensions are,
Radius of gate = 1.2 m, Width of gate = 3.5
m, Density of water = 1000 kg/m3. The
position of the centre of gravity is 4R/3π
horizontally from the origin
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Pressure on a quadrant gate
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Exercise 2: Hydraulic forces on a
rockfill dam
The Government of Uganda intends to construct a rockfill
dam across a valley for water supply and irrigation
purposes. The dam has been designed with a cross
section as shown below and reservoir depth is 12 m.
(i)
Calculate the hydraulic forces on the dam.
(ii)
Determine the location of the centre of pressure
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References
Bansal, R. K. (2005). Fluid Mechanics and Hydraulic Machines. New Delhi: Laxmi
Publications Ltd.
Chadwick, A., Morfett, J., & Borthwick, M. (2013). Hydraulics in Civil and
Environmental Engineering (5th Ed.). London and New York: CRC Pres,
Taylor & Francis Group.
Pasche, E. (2007). Fundamentals of Fluid Mechanics. Hamburg: Hamburg
University of Technology.
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