Download Solution 2/2

FUNDAMENTALS OF
FLUID MECHANICS
Chapter 2 Fluids at Rest
- Pressure and its Effect
1
謝志誠
MAIN TOPICS
 Pressure at a Point
 Basic Equation for Pressure Field
 Pressure variation in a Fluid at Rest
 Standard Atmosphere
 Measurement of Pressure
 Manometry
 Mechanical and Electronic Pressure Measuring Devices
 Hydrostatic Force on a Plane Surface
 Pressure Prism
 Hydrostatic Force on a Curved Surface
 Buoyancy, Floating, and Stability
 Rigid-Body Motion
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1
謝志誠
Pressure at a Point 1/3
Pressure ? Indicating the normal force per unit area at a
given point acting on a given plane within the fluid mass
of interest.
How the pressure at a point varies with the orientation of
the plane passing through the point ?
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謝志誠
Pressure at a Point 2/3
The equation of motion (Newton’s second law, F=ma) in
the y and z direction are,
F
y
 P y δxδz  PS δxδssinθ
F
Z
 P y δxδy  PS δxδscosθ
 y   s cos 
δxδyδz
ay
2
δxδyδz
δxδyδz
-γ
 ρ
az
2
2
 ρ
 z   s sin 
PZ  PS   ρa Z  γ 
δx=0、δy=0、δz=0
δz
2
Py  PS  ρa y
δy
2
PZ  Py  PS
4
2
謝志誠
Pressure at a Point 3/3
The pressure at a point in a fluid ar rest, or in motion, is
independent of the direction as long as there are no
shearing stresses present.
The result is known as Pascal’s law named in honor of
Blaise Pascal (1623-1662).
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謝志誠
Basic Equation for Pressure Field
To obtain an basic equation for pressure field in a static
fluid.
Apply Newton’s second law to a differential fluid mass
 δ F  δma
There are two types of
forces acting on the mass
of fluid: surface force and
body force.
m  V
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3
謝志誠
Body Force on Element



FB  gm  gV


 FB k  xyzk
Where ρ is the density.
g is the local gravitational acceleration.
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謝志誠
Surface Forces 1/4
No shear stresses, the only
surface force is the
pressure force.
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4
謝志誠
Surface Forces 2/4
The pressure at the left face
The pressure at the right face
The pressure force in y direction


 p dy 
 p dy 
p
δF y   p 
δxδyδz
 δxδz   p 
 δxδz  
y 2 
y 2 
y


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謝志誠
Surface Forces 3/4
The pressure force in x direction
p dx 
p dx 
p


δFx   p 
δyδz   p 
δyδz   δxδyδz
x 2 
x 2 
x


The pressure force in z direction
p dz 
p dz 
p


δFz   p 
δxδy   p 
δxδy   δxδyδz
z 2 
z
z 2 


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5
謝志誠
Surface Forces 4/4
The net surface acting on the element
 p
p
p 
δ F s  δF X i  δFZ j  δFZ k   
i
j
k  δxδyδz
y
 z 
 x
gradp  p 
p  p  p 
i
j k
x
y
z
δ F s   gradp( δxδyδz)  pδxδyδz
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謝志誠
General Equation of Motion




F  FS  FB  ( p  g )xyz

 ( p  g )dV


  p  x  y  z   x  y  z k   a  x  y  z
The general equation of motion for a fluid in
which there are no shearing stresses


 p  k  a
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6
謝志誠
Pressure in Static Fluid
For a fluid at rest a=0


 p  k  a  0
p
 g x  0...x  direction
x
p
  g y  0...y  direction
y
p
  g z  0...z  direction
z

g x  0,g y  0,
gz  g
P
0
x
P
0
y
P
 
z
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謝志誠
Pressure-Height Relation
The basic pressure-height relation of static fluid :
Integrated to determine the
pressure distribution in a
static fluid with appropriate
boundary conditions.
Restriction:
Static fluid.
Gravity is the only body force.
The z axis is vertical and upward.
How the specific weight varies with z?
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7
謝志誠
Pressure in Incompressible Fluid
A fluid with constant density is called an incompressible
fluid.

p2
p1
z1
dp    dz
z2
p1 － p2 = γ(z2－z1)=γh
p1=γh +p2
h= z2－z1，h is the depth of fluid
measured downward from the
location of p2.
This type of pressure distribution is
called a hydrostatic distribution.
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謝志誠
Pressure Head in Static Fluid
 The pressure difference between two points in a fluid at rest: p1 －
p2 = γ(z2－z1)=γh
h
p1  p2

h is called the pressure head and is
interpreted as the height of a column of
fluid of specific weight γrequired to give
a pressure difference p1-p2.
 The pressure p at any depth h below the free surface is given by p =
γh + po
The pressure in a homogeneous,
incompressible fluid at rest depends on
the depth of the fluid relative to some
reference plane, and it is not influenced
by the size or shape of the tank or
container in which the fluid is held.
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8
謝志誠
Example 2.1 Pressure-Depth Relationship
 Because of a leak in a buried gasoline storage tank, water has seeped
in to the depth shown in figure. If the specific gravity of the gasoline
is SG=0.68. Determine the pressure at the gasoline-water interface
and at the bottom of the tank. Express the pressure in units of lb/ft2,
lb/in2, and as pressure head in feet of water.
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謝志誠
Solution 1/2
Since we are dealing with liquid at rest, the pressure distribution will be
hydrostatic, and therefor the pressure variation can be found from the equation:
p = γh + po
With po corresponding to the pressure at the free surface of the gasoline, then
the pressure at the interface is
p1  SG H 2O h  p0  (0.68)( 62.4lb / ft 3 )(17ft )  p0
 721  p0 lb / ft 2 
If we measure the pressure relative to atmosphere pressure (gage pressure), it
follows that po =0, and therefore
721lb / ft 2
 5.01lb / in 2
p1  721lb / ft 
2
2
144in / ft
2
p1
721lb / ft

 11.6ft
 H 2O 62.4lb / ft 3
2
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9
謝志誠
Solution 2/2
We can now apply the same relationship to determine the pressure at the tank
bottom; that is,
p2   H 2O h H 2O  p1  (62.4lb / ft 3 )( 3ft )  721lb / ft 2  908lb / ft 2
908lb / ft 2
 6.31lb / in 2
2
2
144in / ft
p2
908lb / ft 2

 14.6ft
 H 2O 62.4lb / ft 3
p2 
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謝志誠
Pressure In Compressible Fluid 1/2
For compressible fluid, ρ=ρ(P,T) , how to determine the
pressure variation?
The density must be expressed as a function of one of the
other variable in the equation.
For example: Determine the pressure variation in the ideal
gas.
p  RT 

p2
p1
dp
p
g z1 dz
 ln 2   
p
p1
R z2 T
dp
gp

dz
RT
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10
謝志誠
Pressure In Compressible Fluid 2/2
  g ( z1  z 2
p 2  p1 exp 
RT o

T=T0=constant
T=To-mz
dp   gdz  
)

pg
pg
dz  
dz
RT
R( To  mz )
z
dp
gdz
 
p1 p
0 R( T  mz )
o

p
ln
p
g
mz

ln( 1 
)
p1 mR
To
 p  p1( 1 
mz g / mR
T g / mR
)
 p1(
)
To
To
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謝志誠
Example 2.2 Incompressible and
Isothermal Pressure-Depth Variations
 The Empire State Building in New York City, one of the tallest
building in the world, rises to a height of approximately 1250ft.
Estimate the ratio of the pressure at the top of the building to the
pressure at its base, assuming the air to be at a common temperature
of 59˚F. Compare this result with that obtained by assuming the air
to be incompressible with =0.0765fb/ft3 at 14.7psi(abs).
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謝志誠
Solution 1/2
For the assumed isothermal conditions, and treating air as a compressible fluid,
Eq. 2.10 can be applied to yield
p2
  g ( z1  z 2 ) 
 exp 

p1
RT o



(32.2ft / s2 )(1250ft )
 exp 
  0.956
(
1716
ft

lb
/
slug


R
)[(
59

460
)

R
]


If the pressure is treated as an incompressible fluid we can apply Eq. 2.5.
In this case
p 2  p1   z 2  z1 
or
p2
 z 2  z1 
(0.765lb / ft 3 )(1250ft )
 1
 1
 0.955
p1
p1
(14.7lb / in 2 )(144in 2 / ft 2 )
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謝志誠
Solution 2/2
Note that there is little difference between the two results. Since the pressure
difference between the bottom and top of the building is small, it follows that the
variation in fluid density is small and, therefore, the compressible fluid and
incompressible fluid analyses yield essentially the same result.
By repeating the calculation, for various values of height, h, the results shown in
figure are obtained.
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謝志誠
Standard Atmosphere1/2
Standard atmosphere was first developed in the 1920s.
The currently accepted Standard atmosphere is based on a
report published in 1962 and updated in 1976.
The so-called U.S. standard atmosphere is an idealized
representation of middle-latitude, year-around mean
conditions of the earth’s atmosphere.
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謝志誠
Standard Atmosphere2/2
For example, in the troposphere,
the temperature variation is of
the form
T = Ta– βz
where Ta is the temperature at
sea level (z=0) and β is the
lapse rate (the rate of change of
temperature with elevation).
 z 
p  pa 1  
 Ta 
g / R
Pa is the absolute pressure at z=0.
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13
謝志誠
Absolute and Gage Pressure
Absolute pressure: measured with respect to vacuum.
Gage pressure: measured with respect to atmospheric
pressure.
p gage  pabsolute  patmosphere
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謝志誠
Example 2.3 Barometric Pressure
 A mountain lake has an average temperature of 10 0C and
a maximum depth of 40 m. For a barometric pressure of
598 mm Hg, determine the absolute pressure (in pascals)
at the deepest part of the lake .
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14
謝志誠
Solution 1/2
The pressure in the lake at any depth, h , is given by the equation
p  h  p 0
Where p0 is the pressure at the surface. Since we want the absolute pressure, p0 will
be the local barometric expressed in a consistent of units ; that is
P barometric
 598 mm  0.598 m
 Hg
And for 
 133kN / m 3
Hg
p 0  (0.598 m)(133 kN / m 3 )  79.5 kN / m 2
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謝志誠
Solution 2/2
From Table B.2,
 H 0  9.804 kN / m3
2
at 10 0C and therefore
p  (9.804 kN / m 3 )( 40 m )  79.5 kN / m 2
 392 kN / m 2  79.5 kN / m 2  472 kPa (abs)
(Ans)
This simple example illustrates the need for close attention to the units used in the
calculation of pressure ; that is, be sure to use a consistent unit systm,and be careful
not to add a pressure head (m) to a pressure (Pa).
30
15
謝志誠
Barometers
Mercury Barometer is used to measure atmosphere
pressure:
Patm＝γh +Pvapor＝γh
Pvapor＝0.000023 lb / in2@68oF
γ：specific weight of mercury
the height of a mercury column is
converted to atmosphere pressure by
using
p atm  p vapor   gh
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謝志誠
Manometry
A standard technique for measuring pressure involves the
use of liquid column in vertical or inclined tubes.
Pressure measuring devices based on this technique are
called manometers.
Piezometer Tube.
U-Tube manometer.
Inclined-Tube manometer.
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16
謝志誠
Piezometer Tube 測壓管計
The fundamental equation is
P = P0 + γh >> PA = γ1 h1
PA : gage pressure ( P0=0)
γ1 :the specific weight of the liquid in the
container
h1: measured from the meniscus at the upper
surface to point(1)
Only suitable if the pressure in the container is
greater than atmospheric pressure, and the pressure to
be measured must be relatively small so the required
height of the column is reasonable. The fluid in the
container must be a liquid rather than a gas.
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謝志誠
Simple U-Tube Manometer
The fluid in the manometer is called the gage fluid.
A(1)(2)(3)Open
PA + γ1 h 1 – γ2h 2 = 0
>> PA =γ2h 2 –γ1 h 1
If pipe A contains a gas
then γ1h 1≒0
>> PA =γ2h 2
EXAMPLE 2.4
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17
謝志誠
Example 2.4 Simple U-Tube Manometer
 A closed tank contains compressed
air and oil (SGoil = 0.90) as is
shown in Fig. E2.4. A U-tube
manometer using mercury (SGoil =
13.6) is connected to the tank as
shown. For column heights h1 = 36
in., h2 = 6 in., and h3 = 9 in.,
determine the pressure reading (in
psi) of the gage.
35
謝志誠
Solution 1/2
Following the general procedure of starting at one end of the manometer
system and working around to the other, we will start at the air-oil interface in
the tank and proceed to the open end where the pressure is zero. The pressure
at level (1) is
p1  pair   oil ( h1  h 2 )
This pressure is equal to the pressure at level (2), since these two points are at the
same elevation in a homogeneous fluid at rest. As we move from level (2) to the
open end, the pressure must decrease by γHgh3, and at the open end the pressure is
zero. Thus, the manometer equation can be expressed as
or
pair   oil ( h1  h 2 )   Hg h 3  0
pair  (SG oil )(  H 2O )( h1  h 2 )  (SG Hg )(  H 2O ) h 3  0
36
18
謝志誠
Solution 2/2
For the values given
 36  6 
9 
pair  (0.9)( 62.4 lb/ft 3 )
ft   (13.6)( 62.4 lb/ft 3 ) ft 
 12

 12 
So that
pair  440 lb/ft 2
Since the specific weight of the air above oil is much smaller than the specific
weight of the oil, the gage should read the pressure we have calculated; that is,
p gage 
440 lb/ft 2
 3.06 psi
144 in. 2 /ft 2
(Ans)
37
謝志誠
Differential U-Tube Manometer
A(1)(2)(3)(4)(5)B
PA＋γ1h1－γ2h2 －γ3h3＝ PB
The pressure difference is
PA－ PB＝γ2h2＋γ3h3－γ1h1
EXAMPLE 2.5
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19
謝志誠
Example 2.5 U-Tube Manometer
 As will be discussed in Chapter 3, the volume rate of flow, Q,
through a pipe can be determined by means of a flow nozzle located
in the pipes as illustrated in Fig. E2.5. the nozzle creates a pressure
drop, pA － pB, along the pipe which is related to the flow through
the equation Q  K p  p , where K is a constant depending on the
pipe and nozzle size. The pressure drop is frequently measured with
a differential U-tube manometer of the type illustrated.
(a) Determine an equation for pA － pB in terms of the specific
weight of the flowing fluid, γ1, the specific weight of the gage fluid,
γ2, and the various heights indicated. (b) For γ1= 9.80kN/m3 , γ2 =
15.6 kN/m3 , h1 = 1.0m, and h2 = 0.5m, what is the value of the
pressure drop, pA － pB?
A
B
39
謝志誠
Solution1/2
(a) Although the fluid in the pipe is moving, the fluids in the columns of the
manometer are at rest so that the pressure variation in the manometer tudes is
hydrostatic. If we start at point A and move vertically upward to level (1), the
pressure will decrease by γ1h1 and will be equal to pressure at (2) and (3). We
can now move from (3) to (4) where the pressure has been further reduced by
γ2h2 . The pressure at levels (4) and (5) are equal, and as we move from (5) to B
the pressure will increase byγ1(h1 + h2). Thus, in equation form
p A   1h1   2 h2   1 (h1  h2 )  pB
or
p A  p B  h2 ( 1   2 )
(Ans)
40
20
謝志誠
Solution2/2
It is to be noted that the only column height of importance is the differential
reading, h2. The differential manometer could be placed 0.5 or 5.0 m above
the pipe (h1 = 0.5m or h1 = 5.0m )and the value of h2 would remain the same.
Relatively large values for the differential reading h2 can be obtained for
small pressure differences, pA－pB , if the difference between γ1 andγ2 is
small.
(b) The specific value of the pressure drop for the data given is
p A  p B  ( 0 .5 m )(15 .6 kN / m 3  9 .80 kN / m 3 )  2 .90 kPa (Ans)
41
謝志誠
Inclined-Tube Manometer
To measure small pressure change, an inclined-tube
manometer is frequently used:
PA +γ1h1 –γ2l2sinθ –γ3h3 = PB
PA – PB =γ2l2sinθ +γ3h3 –γ1h1
If pipe A and B contain a gas thenγ3h3≒γ1h1≒0
>> l2 = ( PA – PB ) /γ2 sinθ
42
21
謝志誠
Mechanical and Electronic Devices
Manometers are not well suited for measuring very high
pressures, or pressures that are changing rapidly with time.
Manometers require the measurement of one or more
column heights, which, although not particularly difficult,
can be time consuming.
Making use of the idea that when a pressure acts on an
elastic structure, the structure will deform, and this
deformation can be related to the magnitude of the
pressure.
43
謝志誠
Bourdon Pressure Gage
Bourdon tube pressure gage uses a hollow, elastic, and
curved tube to measure pressure.
As the pressure within the tube increases the tube tends to
straighten, and although the deformation is small, it can be
translated into the motion of a pointer on dial.
44
22
謝志誠
Aneroid Barometer 無液氣壓計
The Aneroid barometer is used for measuring atmospheric
pressure.
The Aneroid barometer contains a hallow, closed, elastic
elements which is evacuated so that the pressure inside the
element is near absolute zero.
As the external atmospheric pressure changes, the element
deflects, and this motion can be translated into the
movement of an attached dial.
45
謝志誠
Bourdon Gage + LVDT
 Combining a linear variable differential transformer (LVDT) with a
Bourdon pressure gage, converts the pressure into an electric output.
 The core of the LVDT is connected
to the free end of the Bourdon so
that as a pressure is applied, the
resulting motion of the end of the
tube moves the core through the coil
and an output voltage develops.
 This voltage is a linear function of
the pressure and could be recorded
on an oscillograph or digitized for
storage or processing on a computer.
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23
Hydrostatic Forces on a Plane
Surface
謝志誠
Specifying the magnitude of the force.
Specifying the direction of the force.
Specifying the line of action of the force.
To determine completely the resultant force acting on a
submerged force.
47
謝志誠
On a Submerged Surfaces
 The hydrostatic force on any
element of the surface acts
normal to the surface dF = pdA.
 The resultant force
FR   hdA   y sin dA
A
A
Where h=ysin
For constant  and 
FR   sin   ydA
A
First moment of the area wrt the x-axis >>>

A
ydA  yC A
48
24
謝志誠
Resultant Force
The magnitude of the resultant force is equal to pressure
acting at the centroid of the area multiplied by the total
area.
FR  Ayc sin   hc A
yc is the y coordinate of the centroid of the area A.
hc is the vertical distance from the fluid surface to the
centroid of the area.
49
謝志誠
Location of Resultant Force1/2
How to determine the location (xR,yR) of the resultant
force ?
The moment of the resultant force must equal the moment of
the distributed pressure force.
FR y R   ydF    sin y 2dA
A
A
yR


A
y 2 dA
FR  Ayc sin   hc A
I
I
 x  xc  yc
yc A
yc A yc A
The resultant force does
not pass through the
centroid but is always
below it.
Ix is the second moment of the area (moment of inertia).
By parallel axis theorem…
2
I x  I xc  Ayc
50
25
謝志誠
Location of Resultant Force2/2
FR xR   xdF    sin xydA
A
FR  Ayc sin   hc A
A
xR 

A
xydA
yc A

I xy
yc A

I xyc
yc A
 xc
Ixy is the product of inertia wrt the x and y.
By parallel axis theorem… I xy  I xyc  Axc yc
Ixyc is the product of inertia with respect to an orthogonal
coordinate system passing through the centroid of the area and
formed by a translation of the x-y coordinate system.
If the submerged area is symmetrical with respect to an axis
passing through the centroid and parallel to either the x or y
axes, Ixyc=0.
Geometric Properties of Common
Shapes
EXAMPLE 2.6 & 2.7
51
謝志誠
52
26
謝志誠
Example 2.6 Hydrostatic Pressure
Force on a Plane Rectangular Surface
 The 4-m-diameter circular gate of figure (a) is located in the
inclined wall of a large reservoir containing water (=9.80kN/m3).
The gate is mounted on a shaft along its horizontal diameter. For a
water depth hc=10m above the shaft determine : (a) the magnitude
and location of the resultant force exerted on the gate by the water,
and (b) the moment that would have to be applied to the shaft to
open the gate
53
謝志誠
Solution 1/3
(a) To find the magnitude of the force of the water we can apply Eq. 2.18
FR  Ay c sin   h c A
And since the vertical distance from the fluid surface to the centroid of the area is
10m it follows that
FR  (9.80  103 N / m 3 )(10m)( 4 m 2 )  1.23MN
(ans )
To locate the point (center of pressure) through which FR acts, we use Eq. 2.19 and
2.20
I
x R  xy c  x c
ycA
yR


A
y 2 dA
yc A

Ix
I
 xc  yc
yc A yc A
54
27
謝志誠
Solution 2/3
From the coordinate system shown, xR=0 since the area is symmetrical, and the
center of pressure must lie along the diameter A-A. To obtain yR. we have from
Figure 2.18
R 4
4
I xc 
And yc is shown in Fig. b. Thus,
yR 
 / 4 (2m)4
(10m / sin 60)( 4m )
2

10m
 0.0866m  11.55m  11.6m
sin 60
And the distance below the shaft to the center of pressure is
y R  y c  0.0866m
We can conclude that the force on the gate due to the water have a magnitude of
1.23MN and acts through a point along its diameter A-A at a distance of 0.0866m
below the shaft.
55
謝志誠
Solution 3/3
(b) The moment required to open the gate can be obtained with the aid of the freebody diagram of Fig. c. In this diagram W is the weight of the gate and Ox and Oy
are the horizontal and vertical reactions of the shaft on the gate. We can now sum
moments about the shaft
M
c
0
And, therefore,
M  FR y R  y C   (1.23MN )( 0.0866m )  1.07  105 N  m
56
28
謝志誠
Example 2.7 Hydrostatic Pressure Force
on a Plane Triangular Surface
 A large fish-holding tank contains seawater(γ=64.0lb/ft3) to a depth
of 10 ft as shown in Fig. E2.7a. To repair some damage to one
corner of the tank, a triangular section is replaced with a new section
as illustrated. Determine the magnitude and location of the force of
the seawater on this triangular area.
57
謝志誠
Solution 1/3
The various distances needed to solve the problem are shown in Fig.E2.7b. Since the
surface of interest lies in a vertical plane, yc = hc = 9 ft, and from Eq. 2.18 the
magnitude of the force is
FR =γhc A = (64.0 lb/ ft3)(9 ft)(9/2 ft2) = 2590 lb (Ans)
Note that this force is independent of the tank length. The result is the same if the
tank is 0.25ft, 25ft, or 25 miles long. The y coordinate of the center of pressure (CP)
is found from Eq. 2.19,
yR 
I xc
 yc
yc A
And from Fig.2.18
(3ft )( 3ft ) 3 81 4
I xc 
 ft
36
36
58
29
謝志誠
Solution 2/3
So that
yR 
81 / 36ft 4
 9ft
(9ft )( 9 / 2ft 2 )
= 0.0556 ft + 9 ft = 9.06 ft (Ans)
Similarly, from Eq.2.20
And from Fig.2.18
So that
xR 
I xy c 
I xy c
 xc
ycA
81
(3ft )( 3ft ) 2
(3ft )  ft 4
72
72
81 / 72ft 4
xR 
 0  0.0278 ft
(9ft )( 9 / 2ft 2 )
59
謝志誠
Solution 3/3
Thus, we conclude that the center of pressure is 0.0278 ft to the right of and 0.0556 ft
below the centroid of the area. If this point is plotted, we find that it lies on the
median line for the area as illustrated in Fig. E2.7c. Since we can think of the total
area as consisting of a number of small rectangular strips of areaδA (and the fluid
force on each of these small areas acts through its center), it follows that the resultant
of all these parallel forces must lie along the median.
60
30
謝志誠
Pressure Prism
h
FR  pav A     A
2
1
h
 volume  ( h )( bh )     A
2
2
FR  F1  F2
FR y A  F1 y1  F2 y2
y1 
h1  h2
2
y2 
2( h2  h1 )
 h1
3
EXAMPLE 2.8
61
謝志誠
Example 2.8 Use of the Pressure Prism
Concept
 A pressurized contains oil (SG = 0.90) and has a square, 0.6-m by
0.6-m plate bolted to its side, as is illustrated in Fig.E2.8a. When the
pressure gage on the top of the tank reads 50kPa, what is the
magnitude and location of the resultant force on the attached plate?
The outside of the tank is atmospheric pressure.
62
31
謝志誠
Solution 1/3
The pressure distribution acting on the inside surface of the plate is shown in Fig.
E2.8b. The pressure at a given point on the plate is due to the air pressure, ps, at the
oil surface, and the pressure due to the oil, which varies linearly with depth as is
shown in the figure. The resultant force on the plate (having an area A) is due to the
components, F1 and F2 , where F1 and F2 are due to the rectangular and triangular
portions of the pressure distribution, respectively. Thus,
F1  (ps   h1)A
 [50  103 N/m 2  (0.90)(9.8 1  103 N/m3 )(2 m)](0.36m 2 )
 24.4  103 N
63
謝志誠
Solution 2/3
and
0.6m
h1 - h 2
)(0.36m 2 )
) A  (0.90)(9.8 1  103 N/m3 )(
2
2
 0.954  103 N
F2   (
The magnitude of the resultant force, FR, is therefore
FR  F1  F2  25.4  103 N  25.4kN
64
32
謝志誠
Solution 3/3
The vertical location of FR can be obtained by summing moments around an axis
through point O so that
FR y O  F1 (0.3m)  F2 (0.2m)
or
(24.4  103 N)(0.3m)  (0.954  103 N)(0.2m)
25.4  103 N
 0.296m
yO 
Thus, the force acts at a distance of 0.296m above the bottom of the plate along
the vertical axis of symmetry.
Note that the air pressure used in the calculation of the force was gage
pressure. Atmospheric pressure does not affect the resultant force (magnitude or
location), since it acts on both sides of the plate, thereby canceling its effect.
65
謝志誠
On a Curved Surfaces
 Consider the curved section
BC of the open tank.
F1 and F2 can be determined
from the relationships for
planar surfaces.
The weight W is simply the
specific weight of the fluid
times the enclosed volume and
acts through the center of
gravity (CG) of the mass of
fluid contained within the
volume.
FH  F2
FV  F1  W
2
FR  FH  F V
EXAMPLE 2.9
2
66
33
謝志誠
Example 2.9 Hydrostatic Pressure Force
on a Curved Surface
 The 6-ft-diameter drainage conduit of fig. E2.9a is half full of water
at rest. Determine the magnitude and line of action of the resultant
force that the water exerts on a 1-ft length of the curved section BC
of the conduit wall.
67
謝志誠
Solution 1/3
We first isolate a volume of fluid bounded by the curved section BC, the horizontal
surface AB, and the vertical surface AC, as shown in Fig.E2.9b. The volume has a
length of 1 ft.
The forces acting on the volume are the horizontal force F1, which acts on the
vertical surface AC, the weight, W, of the fluid contained within the volume, and the
horizontal and vertical components of the force of the conduit wall on the fluid, FH
and FV, respectively.
The magnitude of F1 is found form the equation
F1  hc A  (62.4lb / ft 3 )(
3
ft )(3 ft 2 )  281lb
2
and this force acts 1 ft above C as shown. The weight, W, is
W  vol  (62.4lb / ft 3 )(9 / 4 ft 2 )(1 ft )  441lb
68
34
謝志誠
Solution 2/3
and acts through the center of gravity of the mass of fluid, which accordingly to Fig.
2.18 is located 1.27 ft to the right of AC as shown. There for, to satisfy equilibrium
FH  F1  281lb
Fv  W  441lb
and the magnitude of the resultant force is
FR 
( FH ) 2  ( FV ) 2

( 281lb ) 2  ( 441lb ) 2  523lb (Ans)
The force the water exerts on the conduit wall is equal, but opposite in direction, to
the force FH and FV shown in Fig. E2.9c. This force acts through the point O at the
angle shown.
69
謝志誠
Solution 3/3
An inspection of this result will show that the line of action of the resultant force
passes through the center of the conduit.
In retrospect, this is not a surprising result since at each point on the curved surface
of the conduit the elemental force due to the pressure is normal to the surface, and
each line of action must pass through the center of the conduit.
It therefore follows that the result of this concurrence force system must also pass
through the center of concurrence of the elemental forces that make up the system.
70
35
謝志誠
BUOYANCY 1/2
Buoyancy: The net vertical force acting on an object
which is immersed in a liquid, or floating on its surface
due to liquid pressure.
Consider a body of arbitrary
shape, having a volume V, that
is immersed in a fluid,
We enclose the body in a
parallelepiped and draw a freebody diagram of parallelpiped
with body removed as shown in
(b).
71
謝志誠
BUOYANCY 2/2
FB  F2  F1  W
F2  F1   ( h2  h1 ) A
FB   ( h2  h1 ) A   ( h2  h1 ) A  V 
FB is the force the body exerting on the fluid.
W is the weight of the shaded fluid volume
(parallelepiped minus body).
A is the horizontal area of the upper (or lower)
surface of the parallelepiped.
For a submerged body, the buoyancy
force of the fluid is equal to the
weight of displaced fluid
Fbuoyancy  gV
72
36
謝志誠
Archimedes’ Principle
For a submerged body, the buoyancy force of the fluid is
equal to the weight of displaced fluid.
Fbuoyancy   g V
The relation reportedly was used by Archimedes in 220
B.C. to determine the gold content in the crown of King
Hiero II.
73
Example 2.10 Buoyant Force on a
Submerged Object
謝志誠
 A spherical buoy has a diameter of 1.5 m, weighs 8.50kN, and is
anchored to the seafloor with a cable as is shown in Fig. E2.10a.
Although the buoy normally floats on the surface, at certain times
the water depth increases so that the buoy is completely immersed
as illustrated. For this condition what is the tension of the cable?
74
37
謝志誠
Solution1/2
We first draw a free-body diagram of the buoy as is shown in Fig. E2.10b, where FB is
the buoyant force acting on the buoy, W is the weight of the buoy, and T is the tension
in the cable. For Equilibrium it follows that
T  FB  W
From Eq. 2.22
FB  V
and for seawater with γ= 10.1 kN/m3 and V = πd3/6 then
FB  ( 10.1  103 N/m 3 ) [(k/6)( 1.5 m) 3 ]  1.785  10 4 N
The tension in the cable can now be calculated as
T  1.785  10 4 N  0.850  10 4 N  9.35kN
(Ans)
75
謝志誠
Solution2/2
Note that we replaced the effect of the hydrostatic pressure force on the
body by the buoyant force, FB. Another correct free-body diagram of the
buoy is shown in Fig. E2.10c. The net effect of the pressure forces on the
surface of the buoy is equal to the upward force of magnitude, FB (the
buoyant force). Do not include both the buoyant force and the hydrostatic
pressure effect in your calculations－use one or the other.
76
38
謝志誠
The Line of Action of FB and C.G.
The line of action of buoyancy force, which may be found
using the method of “hydrostatic force on submerged
surfaces,” acts through the centroid of the displaced
volume.
The point through which the buoyant force acts is called
the center of buoyancy.
C.G: The body force due to gravity on an object act
through its center of gravity (C.G.).
77
謝志誠
Stability
Stability? Stable? Unstable?
A body is said to be in a stable
equilibrium position if, when
displaced, it returns to its
equilibrium position. Conversely, it
is an unstable equilibrium position
if, when displaced (even slightly), it
moves to a new equilibrium
position.
78
39
謝志誠
Stability of Immersed Body
The location of the line of action of
the buoyancy force determines
stability.
While C.G. is below the center of
buoyancy, a rotation from its
equilibrium position will create a
restoring couple formed by the
weight and the buoyancy force.
If C.G. is above the center of
buoyancy,…..
79
謝志誠
Stability of Floating Body
The determination of
stability depends in a
complicated fashion on the
particular geometry and
weight distribution of the
body.
80
40
謝志誠
Rigid-Body Motion
The entire fluid moves as if it were a rigid body –
individual fluid particles, although they may be in motion,
are not deforming. This means that there are no shear
stresses, as in the case of a static fluid.
The general equation of motion


  p   k  a  0
p
 a x
x
p

 a y
y
p
   a z

z

Based on rectangular
coordinates with the
positive z axis being
vertically upward.
81
謝志誠
Linear Motion
p
  a x  0
x
p
  a y
y
p
   ( g  az )
z
The change in pressure
between two closely
spaced points located at y,
z, and y+dy , z+dz
p
p
dy  dz
y
z
dp   a y dy   ( g  a z )dz
dp 
Along a line of constant pressure, dp=0
ay
dz

dy
g  az
EXAMPLE 2.11
82
41
謝志誠
Angular Motion1/2
In terms of cylindrical coordinates, the pressure gradient
can be expressed
p 
p
1 p
p
er 
e  ez ar   rw2êr
r
r 
z
The differential pressure is dp 
a  0
az  0
p
p
dr  dz  r 2dr  dz
r
z
83
謝志誠
Angular Motion 2/2
Along a line of constant pressure, dp=0
The equation for surface of constant pressure is
dz r 2
r 2 2

z
 cons tan t
dr
g
2g
The equation reveals that the surfaces of constant
pressure are parabolic
The pressure distribution in
a rotating liquid
p
p
dr  dz  r 2dr  dz
r
z
r 2 2
int egration  p 
 z  cons tan t
2
dp 
EXAMPLE 2.12
84
42
謝志誠
Example 2.11 Pressure Variation in an
acceleration tank
 The cross section for the fuel tank of an experimental vehicle is
shown in Fig. E2.11. the rectangular tank is vented to the
atmosphere, and a pressure transducer is located in its side as
illustrated. During testing of the vehicle, the tank is subjected to be a
constant linear acceleration, ay.
(a) Determine an expression that
relates ay and the pressure( in
lb/ft2) at the transducer for a
fuel with a SG = 0.65.
(b) What is the maximum
acceleration that can occur
before the fuel level drops
below the transducer?
85
謝志誠
Solution1/3
(a) For a constant horizontal acceleration the fuel will move as a rigid body,
and from Eq.2.28 the slope of the surface can be expressed as
a
dz
 y
dy
g
Since az = 0. Thus for some arbitrary ay, the change in depth, z1, of liquid on the right
side of the tank can be from the equation
a
z1
 y
0.75ft
g
or
a 
z 1  (0.75ft ) y 
g

86
43
謝志誠
Solution2/3
Since there is no acceleration in the vertical, z, direction, the pressure along the wall
varies hydrostatically as shown by Eq.2.26. Thus, the pressure at the transducer is
given by the relationship
p  h
Where h is the depth of fuel above the transducer, and therefore
p  (0.65)( 62.4lb / ft 3 )[0.5ft  (0.75ft )( a y / g)]  20.3  30.4
ay
g
For z1≦0.5 ft. as written, p would be given in lb/ft2.
87
謝志誠
Solution3/3
(b) The limiting value for (ay)max (when the fuel level reaches the transducer)
can be found from the equation
2g
 (a ) 
0.5ft  (0.75ft )  y m ax  or (a y ) m ax 
3
 g 
And for standard acceleration of gravity
2
(a y ) max  (32.2ft / s2 )  21.5ft / s 2
3
Note that the pressure in horizontal layers is not constant in this
example since p/ y=-ay ≠0. thus, for example , p1≠p2
88
44
謝志誠
Example 2.12 Free Surface Shape of
Liquid in a Rotating Tank
 It has been suggested that the angular velocity, , of a rotating body
or shaft can be measured by attaching an open cylinder of liquid, as
shown in figure, and measuring with some type of depth gage the
changes in the fluid level, H-ho, caused by the rotation of the fluid.
Determine the relationship between this change in fluid level and the
angular velocity.
89
謝志誠
Solution 1/2
The height, h, of the free surface above the tank bottom can be determined from
h
2 r 2
 h0
2g
The initial volume of fluid in the tank is equal to
Vi  R 2 H
The volume of the fluid with the rotating tank can be found with the aid of the
differential element shown in Fig. b. This cylindrical shell is taken at some
arbitrary radius, r, and its volume is
dV  2rhdr
90
45
謝志誠
Solution 2/2
The total volume, is , therefore
2 2
R  r

2 R 4
V  2  r 
 h 0 dr 
 R 2 h 0
0
4
g
2
g


Since the volume of the fluid in the tank must remain constant, it follows that
2 R 4
R H 
 R 2 h 0
4g
2
or
2 R 2
H  h0 
4g
This is the relationship we were looking for. It shows that the change in depth
could indeed be used to determine the rotational speed, although the relationship
between the change in depth and speed is not a linear one.
91
46