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Thermofluids Notes on Fluid Statics and Work and Heat.
Typology: Slides
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Chapter 2: Fluid Statics
G. Mazzanti
Process Engineering and Applied Science
Dalhousie University
Fall 2019
Slides by Michele Hastie, 2016
Slide 13 (page 31): Added diagram
Added Slide 28
Outline
2.1 Pressure
2.2 Pressure-Elevation Relationships
2.3 Manometers
2.4 Buoyancy and Stability
2.5 Hydrostatic Forces of Submerged Surfaces
2.6 Tank Failures
2.7 Problems
We will not cover
this section.
2.1 Pressure (page 26)
Pressure – the effect of a
normal force acting on an area
When a force Δ F acts at an
angle to an area Δ A it is only
the normal component Δ Fn
that is used to define pressure:
Common units of pressure:
A
F P
n
A (^)
→ 0
lim
2.1 Pressure (page 26)
Relative to pressure in a perfect
vacuum
Relative to atmospheric pressure
Most calculations require absolute
pressure ( e.g ., ideal gas law).
When calculating a change in
pressure, either gauge or absolute
pressure can be used ( e.g .,
pressure-depth equation).
Pabs = Patm + Pgauge
2.2 Pressure-Elevation Relationships (page 28)
Consider a small volume
(Δ x Δ y Δ z ) in a large mass
of fluid at rest.
Since the fluid is at rest, the sum of all the forces must be
zero.
Force balance in the z - direction:
Dividing by Δ x Δ y Δ z :
( Pz (^) = 0 ) x y −( Pz = z ) x y = g x y z
g
z
Pz (^) z Pz = −
= −^ = 0 g s
dz
dP = − = −
Specific weight
2.2 Pressure-Elevation Relationships (page 29)
Patm
P 1
P 2
P 3
Mercury
Water
Pressure is greater in mercury (does not equal P 3 )
2.2 Pressure-Elevation Relationships (page 29)
2.2.1 Constant Density
Pressure can be measured in terms of fluid height.
Invention of the mercury barometer is credited to
Torricelli (1608–1647).
http://ap-physics.david-s.org/simple-mercury-barometer/
kg
m
kg 13595
Pa
N m 101325 Pa
3
2
2 1
−
h
P g h
P P g h
atm^
2.2 Pressure-Elevation Relationships (page 31)
Example 2.1: What pressure would a
diver experience at a depth of 200 ft?
The water may be considered
incompressible with a density of
62.4 lbm/ft
3
. Work entirely in fps units.
c c
g g P P z z h g g
− = − − =
2 1 c
g P P h g
= +
( )
2 m (^2 ) m 2 f
ft
lb (^) s 14.7 psi 62.4 200 ft ft ft lb
lb s
P
= + ^ (^)
2 f (^2 2 )
lb ft 14.7 psi 12480 ft 144 in
P
^ = + (^)
P 2 (^) = 14.7 psi +86.7 psi P 2 (^) =101.4 psia (absolute)
sea level
increasing elevation
u
2.2 Pressure-Elevation Relationships (page 31)
(2.12)
( 2 1 )
1
2 ln z z RT
gM
u
2
1
2
1
P
P
z
u z
dz RT
gM
dP
gM z P P
u
2 1 exp (2.13)
g dz
dP
Note: Density is not
constant because it depends
on pressure.
2.2 Pressure-Elevation Relationships (page 32 )
2.2.3 Isentropic, Perfect Gas (Ideal Gas)
For a perfect gas undergoing an isentropic
process, the pressure-density relationship is:
Note that: and
Therefore:
k k Pv P
− = constant =
k
s
s
P
P
1
0 0 0
= =
=
3
3
m
kg
1
kg
m
v v
p
c
c k =
0 0 =^ =constant
− k − k P P
k
P
P
1
0
(^0)
= (2.14)
Need an
expression for ρ
as a function of P.
2.3 Manometers (page 38)
Manometer – device that uses a column of liquid to
measure pressure.
h
Patm
Pressure
Vessel
( ) 2 1 2 1
P − P = P = − g z − z
P 2 , z 2
P 1 , z 2
1
P gh gx gx P atm
2.3 Manometers (page 39)
P 1 = Patm + gh
atm m o
P P gh gh
P P gh gh gh
= + − −
= + − −
3
3
P P ( ) gh
P P gh gh gh gh
m
o m o
= + −
= + + − −
5 4
5 4
atm m o
P P gh gh
P P gh gh gh
= + − −
= + − −
6
6
P 2 = Patm + gh
2.4 Buoyancy and Stability (page 41 )
Archimedes Principle:
For an object to remain at rest within the fluid (neutrally
buoyant), the weight ( W ) must be balanced by the
buoyant force:
f displaced
W = gV
Fabove
Fbelow
Fabove = Weight from fluid above
Fbelow Fbelow = Weight from fluid above
Fabove
Fabove
Fbelow
Fabove = Weight from fluid above
Fbelow Fbelow = Weight from fluid above
Fabove
2.4 Buoyancy and Stability (page 41)
Archimedes Principle:
For an object to remain at rest at the surface, the weight
of an object ( W ) must be balanced by the buoyant force:
Only weight of liquid
is considered
because ρ liquid >> ρ gas
f displaced
W = gV