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Fluid Statics: Pressure, Buoyancy, and Tank Failures, Slides of Thermodynamics

Thermofluids Notes on Fluid Statics and Work and Heat.

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ENGI 2102 Thermo-Fluid Engineering I
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
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Download Fluid Statics: Pressure, Buoyancy, and Tank Failures and more Slides Thermodynamics in PDF only on Docsity!

ENGI 2102 Thermo-Fluid Engineering I

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

 2.2.1 Constant Density

 2.2.2 Isothermal, Perfect Gas

 2.2.3 Isentropic, Perfect Gas

 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:

 101325 Pa = 101.325 kPa = 1.01325 bar = 1 atm = 14.696 psi

= 760 mmHg

A

F P

n

A (^) 

 → 0

lim

2.1 Pressure (page 26)

 Absolute pressure scale:

 Relative to pressure in a perfect

vacuum

 Gauge pressure scale:

 Relative to atmospheric pressure

 It is often more convenient to

measure values in gauge

pressure.

 Calculations:

 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

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 )   xy −( Pz = z ) xy =  gxyz

g

z

Pz (^) z Pz = − 

=  −^ = 0 g s

dz

dP = − = − 

Specific weight

2.2 Pressure-Elevation Relationships (page 29)

 Stevin’s Law – the pressure is the same at all points on a

horizontal plane in a particular fluid irrespective of geometry

as long as the points are connected by the same fluid.

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).

 1 mmHg = 1 Torr = 1/760 atm

http://ap-physics.david-s.org/simple-mercury-barometer/

  1. 760 m 760 mmHg

kg

N

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.

2 1 (^2 1 ) (2.10)

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

2.2.2 Isothermal, Perfect Gas (Ideal Gas)

 For gases at low pressure, the density

changes according to the ideal gas law:

 Plugging this into Equation (2.9) and integrating:

R T
PM

u

2.2 Pressure-Elevation Relationships (page 31)

(2.12)

( 2 1 )

1

2 ln z z RT

gM

P
P

u

 

2

1

2

1

P

P

z

u z

dz RT

gM

P

dP

R T

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

kk PP

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

PP =  P = − g zz

h

P 2 , z 2

P 1 , z 2

1

P gh gx gx P atm

  •  + − =
  • Start at a point where you

know the pressure (in this

case, Patm ).

  • Work your way to the other

pressure by ± ρgh.

  • Decrease in elevation: +
  • Increase in elevation: –

2.3 Manometers (page 39)

P 1 = Patm +  gh

atm (^ m )^ o

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

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:

 An immersed object in a fluid experiences a vertical buoyant

force equal to the weight of fluid is displaces.

 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:

 A floating object displaces its own weight in fluid in which it is

floating.

 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