FLUID FLOW
Continuity Equation
For a incompressible fluid like water the
following formula is applicable:
A1 . v1 = A2
. v2
Where ;
A = cross
sectional area (m2) A = ( p . d 2 ) /4
v = velocity
(m/s)
Also
Q = A . v
Where Q = Volume
flow rate (m3/s)
Therefore in a section of fluid flow from
point 1 to point 2 with no branches or leaks and constant volume flow: Q1
= Q2
Bernoulli Equation:
A fluid such as water contains energy.
The three forms of energy that are relevant
are:
1. Potential energy
2. Pressure energy
3. Kinetic energy.
It is more convenient to use the forms of
energy in values of energy head as shown below;
z 1 + ( p1 / r.g ) + ( v12 / 2 . g ) = z
2 + ( p2 / r.g ) + ( v22 / 2 . g )
Where;
z = height or potential head (m)
p = pressure (N/m2)
r = density of water (1000 kg/m3)
g = acceleration due to gravity (9.81 m/s2)
v = fluid velocity (m/s)
In fluid flow examples, if a section of flow
is examined, then the change in energy head between point 1 and 2 is as shown
below.
In some examples the section of flow to be
examined is a horizontal component therefore the height value (z) does not
change and may be omitted from the formula, as shown below.
( p1 / r.g ) + ( v12 / 2 . g ) = (
p2 / r.g ) + ( v22 / 2 . g )
Where;
p = pressure (N/m2)
r = density of water (1000 kg/m3)
g = acceleration due to gravity (9.81 m/s2)
v = fluid velocity (m/s)
EXAMPLE 1
A horizontal water pipe contains a uniform
concentric taper where the diameter reduces from 400mm to 200mm.
The water pressure at the inlet of the taper
is 1 bar or (100 kN/m2) or (100,000 N/m2)
If the inlet velocity is 2 m/s calculate the
outlet velocity and the final pressure (in bar) at the outlet.
Continuity Equation:
A1 . v1 = A2
. v2
Find A1:
Cross sectional area = ( p . d 2 ) /4
A1 = ( p . d 2 ) /4 = ( p . 0.4 2 )
/ 4 = 0.1257 m2
Q1 =
0.1257 x 2.0 = 0.2514 m/s = Q2
A2 = ( p . 0.2 2 )
/ 4 = 0.0314 m2
v 2 = Q2 / A2
v 2 = 0.2514 \ 0.0314 = 8.0 m/s
Use Bernoulli to find p2.
( p1 / r.g ) + ( v12 / 2 . g ) = (
p2 / r.g ) + ( v22 / 2 . g )
There is no z value because the taper is
horizontal.
(100,000 / 1000 x 9.81) + (22 / 2 x 9.81) = (
p 2 / 9810 ) + 82
/ 2 x 9.81)
10.194 + 0.204 = ( p 2 / 9810 ) + 3.262
7.136 = p
2 / 9810
p
2 = 70,004 N/m2. = 0.7 bar
NOTE: 100,000 N/m2.
= 1.0 bar
EXAMPLE 2
A water pipe tapers from 300mm to 150mm.
The pressure at the inlet is 500 kN/m2.
The mean flow velocity at the inlet is 3.2
m/s.
The elevation of the 300mm section is 4
metres above the 150mm section.
Using Bernoulli’s equation find:
(a)
the mean flow velocity at the 150mm section.
(b) the kinetic head at the 150mm section.
Answer (a)
Q2 = Q1
Q1 = A1 . v1.
A1 . v1 = A2
. v2
A1 = ( p . d 2 ) / 4 = ( p . 0.3 2 )
/ 4 = 0.0707 m2
Q1 = 0.0707 x 3.2 = 0.226
m3/s = Q2
v 2 = Q2 / A2
v 2 = 0.226 / ( p . 0.15 2 ) / 4 = 12.79 m/s.
Answer (b)
Kinetic head = ( v12 / 2 . g)
= 12.79 2 / 2 x 9.81
= 8.338 m
EXAMPLE 3
A horizontal water pipe contains a uniform
concentric taper where the diameter reduces from 300mm to 80mm.
The water pressure at the inlet of the taper
is 5 bar.
If the inlet velocity is 2 m/s calculate the
outlet velocity and the final pressure (in bar) at the outlet.
Continuity Eqn.
A1 . v1 = A2
. v2
A1 = ( p . d 2 ) / 4 = ( p . 0.30 2 ) / 4 = 0.0707 m2
A2 = ( p . d 2 ) / 4 = ( p . 0.08 2 ) / 4 = 0.00503 m2
A1 . v1 = A2
. v2
0.0707 x 2.0 = 0.00503
x v 2
v 2 = 28.11
m/s
(
p1 / r.g ) + ( v12 / 2 . g ) = (
p2 / r.g ) + ( v22 / 2 . g )
where;
z = height or potential head (m)
p = pressure (N/m2)
r = density of water (1000 kg/m3)
g = acceleration due to gravity (9.81 m/s2)
v = fluid velocity (m/s)
50.968
+ 0.204 = ( p 2 / 9810 ) + 40.274
p 2 / 9810 = 10.898
p
2 = 106,909 N/m2.
p
2 = 1.069 bar.
EXAMPLE 4
A horizontal water pipe contains a uniform
concentric taper where the diameter reduces from 250mm to 150mm.
The water pressure at the inlet of the taper
is 0.6 bar.
If the inlet velocity is 0.8 m/s calculate
the outlet velocity and the final pressure (in bar) at the outlet.
z 1 + ( p1 / r.g ) + ( v12 / 2 . g ) = z
2 + ( p2 / r.g ) + ( v22 / 2 . g )
Answer:
Velocity at outlet = 2.22 m/s
Pressure at outlet = 0.579 bar