Cu06997 lecture 9_open channel
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Transcript of Cu06997 lecture 9_open channel
CU06997 Fluid Dynamics
Open channel flow 1 5.1 Flow with a free surface (page 122)
5.2 Flow classification (page 122, 123)
5.3 Channels and their properties (page 123-125)
5.4 Velocity distributions (page 126,127)
5.5 Laminar and turbulent flow (page 127-129)
5.6 Uniform flow (page 129 -138)
1
Flow with a free surface
1
Classification of flows, see part 2
1. Steady uniform flow example: pipe with constant D and Q
example: channel with constant A and Q
2. Steady non-uniform flow example: pipe with different D and constant Q
example: channel with different A and constant Q
3. Unsteady uniform flow example: channel with constant A and different Q
4. Unsteady non-uniform flow example; channel with different A and Q
2
Types of flow
2
Geometric properties
3
Velocity distributions
3
Velocity distributions
πππ£πππππ =π
π΄=
π1π΄1 + π2π΄2 + π3π΄3
π΄1 + π΄2 + π΄3
ππ‘ππ‘πππ = π1 + π3 + π3=π1π΄1 + π2π΄2 + π3π΄3
3
Reynolds number, see part 3
π = Absolute viscosity [m2/s]
π = Kinematic viscosity [kg/ms]
water, 20Β°C= 1,00 β 10β6
π = Density of liquid [kg/m3]
π = Velocity [m/s]
D = Hydraulic diameter [m]
R = Hydraulic Radius = D/4 [m]
π π = Reynolds Number [1]
πΉπ > ππππ Turbulent flow
πΉπ < ππππ Laminar flow
π π =π. π·
π
π π =π. 4π
π
In this course we only look at turbulent flow 3
Open channel, with bed slope >0
2211 AuAuQ
Head loss
Reference line
π¦1 + π§1 +π’1
2
2π= π¦2 + π§2 +
π’22
2π+ βπ»1β2
4
u1
Reference [m]
Surfacelevel y +z [m]
Total Head H [m]
P1
z1
y1
u12/2g
P2 z2
y2
u22/2g
u2
21
2
222
2
111
22 H
g
uzy
g
uzy
Head loss [m] ΞH
Velocity Head [m]
Open channel, with bed slope <= 0
4
Length
Chezy formula
Chezy formula describes the mean velocity of uniform, turbulent flow
ΞH
π = πΆ β π β ππ
π = Mean Fluid Velocity [m/s]
R = Hydraulic Radius [m]
ππ = Hydraulic gradient [1]
πΆ =8π
π Chezy coefficient [m1/2/s]
ππ =ΞH
πΏ
5
Chezy coefficient
/s][m 12
log18 1/2
k
RC
In this course we assume a hydraulic rough boundary
Boundary hydraulic rough
kS = surface roughness [m]
5
Surface roughness kS [m] Equivalent Sand Roughness,
Material (ft) (mm)
Copper, brass 1x10-4 - 3x10-3 3.05x10-2 - 0.9
Wrought iron,
steel 1.5x10-4 - 8x10-3 4.6x10-2 - 2.4
Asphalt-lined
cast iron 4x10-4 - 7x10-3 0.1 - 2.1
Galvanized iron 3.3x10-4 - 1.5x10-
2 0.102 - 4.6
Cast iron 8x10-4 - 1.8x10-2 0.2 - 5.5
Concrete 10-3 - 10-2 0.3 - 3.0
Uncoated Cast
Iron 7.4x10-4 0.226
Coated Cast Iron 3.3x10-4 0.102
Coated Spun
Iron 1.8x10-4 5.6x10-2
Cement 1.3x10-3 - 4x10-3 0.4 - 1.2s
Wrought Iron 1.7x10-4 5x10-2
Uncoated Steel 9.2x10-5 2.8x10-2
Coated Steel 1.8x10-4 5.8x10-2
Wood Stave 6x10-4 - 3x10-3 0.2 - 0.9
PVC 5x10-6 1.5x10-3
Compiled from Lamont (1981), Moody (1944), and
Mays (1999)
5
Manningβs formula
π =π
23 β ππ
12
π π =
1
πβ
π΄53
π23
β ππ
12
π = Mean Fluid Velocity [m/s]
R = Hydraulic Radius [m]
ππ = Slope Total head [1]
π΄ = Wetted Area [m2]
π = Wetter Perimeter [m]
π = Mannings roughness coefficient [s/m1/3]
n
RC
61
Manningβs formula describes the
mean velocity of uniform,
turbulent flow
6
Manning's roughness coefficient
6
Mean boundary shear stress
π0 = π β π β π β π0
Ο0 = shear stress at solid boundary [N/m2]
R = Hydraulic Radius [m]
π0 = Slope of channel bed [1]
7
Flowing water and energy
][2
2
1111 m
g
uyzH
u1
Reference /datum [m]
Surface level [m]
Total head H [m]
P1
z1
y1
u12/2g Velocity head [m]
y = Pressure head [m]
z = Potential head [m]
Specific Energy
V
Channel bed as datum [m]
Surface level [m]
Total head H or Specific energy Es [m]
y
V2/2g Velocity head [m]
y = Pressure head [m]
= water depth [m]
πΈπ = π¦ + π2
2π
π = Mean Fluid Velocity [m/s]
y =p
Οβg= Pressure Head / water depth [m]
8
Equilibrium / normal depth
Discharge, cross-section, energy
gradient and friction are constant
yyb
yb
P
AR
2
.
Side view
Cross-section
π = πΆ β π β ππ
π = π β π΄ = πΆ π¦ β ππ2 β π¦ β π
π0 = ππ
yn
yn
π¦π =π2
π2 β πΆ2 β π0
3
9
Equilibrium / normal depth
π¦π =π2
π2 β πΆ2 β π0
3
yn = normal depth [m]
q = discharge [m3/s]
b = width [m]
π0 = bed slope [1]
ππ = Hydraulic gradient caused by friction [1]
πΆ =8π
π Chezy coefficient [m1/2/s]
π0 = ππ
9
Equilibrium / normal depth
Dredged area
π¦π =π2
π2 β πΆ2 β π0
3
yn
yn
yn
yn
9