Upload
nichupan-pratheeprat
View
213
Download
0
Embed Size (px)
Citation preview
7/25/2019 Fluid slide
1/16
9/22/2015
1
4 (Bernoulli Equation)
Daniel Bernoulli (1700 1782)
Born 8 February 1700:
Broningen, Netherlands
Died 8 March 1782 (aged 82):
Basel, Switzerland
Residence Trizzy
Known for Bernoulli's
Principle, early Kinetic theory
of gases, Thermodynamics
Intro. Fluid Mechanics 2
7/25/2019 Fluid slide
2/16
9/22/2015
2
First Published Bernoullis principle Bernoulli's principle
is named after the
Dutch-Swiss
mathematician
Daniel Bernoulli
who published his
principle in his
bookHyd odynam ca in
1738.
Intro. Fluid Mechanics 3
Intro. Fluid Mechanics 4
(Bernoulli Equation)
(frictionless flow, inviscid flow)
2
constant (J/k2
g)p V
gz
7/25/2019 Fluid slide
3/16
9/22/2015
3
Intro. Fluid Mechanics 5
(Bernoulli Equation)
Intro. Fluid Mechanics 6
(Bernoulli Equation)
valid
7/25/2019 Fluid slide
4/16
9/22/2015
4
Intro. Fluid Mechanics 7
(Bernoulli Equation)
valid
Intro. Fluid Mechanics 8
(Bernoulli Equation)
net net system
cv cs
Q W e d e V dAt
4
1. (shaft work) CS
2. (normal stress work)
3. (viscouse stress work)
4. (other work)
7/25/2019 Fluid slide
5/16
9/22/2015
5
Intro. Fluid Mechanics 9
steady state, incompressible flow, frictionless flow inviscid flow,,- 1 intensive properties
(Bernoulli Equation)
2 2
2 2 1 1, 2 2 1 12 2
net shaft net
p V p Vq w u gz u gz
net shaft shear other net
cv cs
pQ W W W e d e V dA
t
2 2
1 1 2 2, 1 2 2 1
2 2shaft net net
p V p Vw gz gz u u q
Intro. Fluid Mechanics 10
(Bernoulli Equation)
2 2
1 1 2 2, 1 2 2 1
2 2shaft net net
p V p Vw gz gz u u q
4
2 2
1 1 2 21 2
2 2
p V p Vgz gz
2constant
2
p Vgz
7/25/2019 Fluid slide
6/16
9/22/2015
6
Intro. Fluid Mechanics 11
(Bernoulli Equation)
2
( kgJ/ )2
p Vgz const
Intro. Fluid Mechanics 12
(mechanical energy per unit mass of working fluid)
2 2
1 1 2 21 2
(J/ )2 2
kgp V p V
gz gz
2
2
V
gz
(flow energy)
(kinetic energy)
(potential energy)
(Bernoulli Equation)
7/25/2019 Fluid slide
7/16
9/22/2015
7
Intro. Fluid Mechanics 13
(mechanical energyper unit weight)
(Bernoulli Equation)
2 2
1 1 2 21 2
= (J/ m)2 2
Np V p V
z z Hg g g g
2
2
V
g
z
(pressure head)
(velocity head)
(elevation head)
H (total head)
Intro. Fluid Mechanics 14
(Bernoulli Equation)
2 2
1 1 2 2 = (J/ m)2 2
Np V p V
Hg g g g
7/25/2019 Fluid slide
8/16
9/22/2015
8
Intro. Fluid Mechanics 15
(Bernoulli Equation)
2 221 2
1 1 2 2 (N/m )2 2
V Vp gz p gz
2
2
V
z
(static pressure)
(dynamic pressure)
(hydrostatic pressure)
Intro. Fluid Mechanics 16
: 4.1
0.1 0.02 m2 50 m/s
7/25/2019 Fluid slide
9/16
9/22/2015
9
4.1
Intro. Fluid Mechanics 17
2 21 21 2
( ) ( )
2 2
atm g atm g P P P Pv v
g g g g
2 21 21 2
( ) ( )
2 2
g gP Pv v
g g g g
23
2 2 2 2 31 2 1 2
1.0
50 10 1.2 102 2
g
kg
g mmP v v Pag s
2
3 2 2 2 2
.
. .
kg m kg kg m
m s m s m s
1 2m m
1 1 2 2A v A v 2
2 2 21 2
1 1
A v Dv v
A D
1
0.02 5010 /
0.1v m s
Intro. Fluid Mechanics 18
: 4.2
1 m 7 m
7/25/2019 Fluid slide
10/16
9/22/2015
10
4.2
(1) (Steady flow)
(2) (Incompressible flow)
(3) (Inviscid fluid)
(4) (5) (V
1= 0)
Intro. Fluid Mechanics 19
2
2
221
2
11
22gz
vPgz
vP
4.2() 1 2
1 2
P1
= P2
V1 V
1= 0
Intro. Fluid Mechanics 20
smms
mzzgv
gzv
gz
gz
vP
gz
vP
/7.117807.92)(2
2
22
2212
2
2
21
2
2
22
1
2
11
7/25/2019 Fluid slide
11/16
9/22/2015
11
4.2() A 1
Continuity equation VA
= V2
V1 V
1= 0
Intro. Fluid Mechanics 21}5.78{8.22
.
.)1(807.91000
.
.
2
7.111000)10013.1(
)(2
)(2
22
0;
22
)(
2
23
2
2
22
32
5
1
2
21
1
2
21
1
2
11
2
2
12
1
2
11
2
gageabs
AA
AA
AA
A
AAA
kPakPa
mkg
sNm
s
m
m
kg
mkg
sN
s
m
m
kg
m
N
zzgv
PP
zzgvPP
gzvP
gzvP
vvv
gzvP
gzvP
Intro. Fluid Mechanics 22
: 4.3
0.45 m 50mm (uniform flow)
2
7/25/2019 Fluid slide
12/16
9/22/2015
12
Intro. Fluid Mechanics 23
: 4.4
2 2
1 1 2 21 2
(J/ )2 2
kgp V p V
gz gz
1 1atmp gD 2 2atmp p gD
2 2
1 21 2
2 2
atm atmp gD p gDV V
2 2
1 21 2
2 2
V VD gD
Intro. Fluid Mechanics 24
: 4.4
2 2
1 21 2
2 2
V VD gD
2 1 22
2 9.81 0.45 0.005
2.8 m s
V g D D
7/25/2019 Fluid slide
13/16
9/22/2015
13
Intro. Fluid Mechanics 25
: 4.4
540 mm2 10 kW
3 m
Intro. Fluid Mechanics 26
:
Wall pressure tab Static pressure probe
7/25/2019 Fluid slide
14/16
9/22/2015
14
Intro. Fluid Mechanics 27
: (stagnation pressure)
22 (N/m )
2stag
Vp p
2 2
2 2
stag
stag
V Vp p
Intro. Fluid Mechanics 28
pitot tube Pitot
: (stagnation pressure)
Henry de Pitot (1695-1771)
7/25/2019 Fluid slide
15/16
9/22/2015
15
A flow of air into a venturi meter. The
kinetic energy increases at the
expense of the fluid pressure, as
shown by the difference in height of
the two columns of water.
This article is about Bernoulli's principle and Bernoulli's equation in fluid dynamics.
For an unrelated topic in ordinary differential equations, see Bernoulli differential
equation.
A flow of air into a venturi meter. The kinetic energy increases at the expense of the
fluid pressure, as shown by the difference in height of the two columns of water.In
fluid dynamics, Bernoulli's principle states that for an inviscid flow, an increase in
the speed of the fluid occurs simultaneously with a decrease in pressure or a
decrease in the fluid's potential energy.[1][2]Intro. Fluid Mechanics 29
Intro. Fluid Mechanics 30
3
:
22 (N/m )
2stag
Vp p
7/25/2019 Fluid slide
16/16
9/22/2015
16
Intro. Fluid Mechanics 31
: Pitot-Static Probe
Intro. Fluid Mechanics 32
: 4.5
pitottube static tube
30 mm