VENTURIMETER
• It isa device used to measure
the rate of flow of a fluid
flowing through a pipe.
• It consists of 3 parts
a. A short converging part
b. Throat
c. Diverging part.
4.
Expression for rateof flow through venturi meter.
• Consider a venturi meter fitted in a
horizontal pipe through which a fluid
is flowing.
• Let d1 = diameter at inlet or at
section (1)
p1 = pressure at section (1)
v1 = velocity of fluid at section
(1)
a1 = area at section (1)
• And, d2, p2, v2, a2 are the
corresponding values at section (2)
5.
Venturi meter
• ApplyingBernoulli’s equation at section (1) and (2), we get
• As the pipe is horizontal, hence z1=z2
Venturi meter
Value of‘b’ given by differential U-tube manometer
CASE 01: Let the differential manometer contains a
liquid which is heavier that the liquid flowing through the
pipe.
Let Sh = Sp. Gravity of the heavier liquid
So = Sp. Gravity of the liquid flowing through pipe
x = Difference of the heavier liquid column in U-tube
Then:
8.
Venturi meter
CASE 02.If the differential manometer contains a liquid
which is lighter than the liquid flowing through the pipe,
the value of h is given by
Where:
St = Sp. gr. of the lighter liquid in U-tube
So = Sp. gr. of fluid flowing through the pipe
x = Difference of the lighter liquid columns in U-tube
9.
Venturi meter
• CASE03. Inclined venturi meter with Differential U-
Tube manometer.
Case 01 and 02 are given for a horizontal venturi
meter. This case is related to inclined venturi meter having
differential U-tube manometer. Let the differential
manometer contains heavier liquid then h is given as
• CASE 04. Similarly, for inclined venturi meter in which
differential manometer contains a liquid which is lighter
than the liquid flowing through the pipe, the value of h is
given as
10.
ORIFICE METER/ORIFICE PLATE
•It is a device used for measuring the
rate of flow of a fluid through a pipe.
• Cheaper device as compared to
venturi
meter.
• Orifice- flat circular plate which has
circular sharp edged hole, which is
concentric with the pipe.
• The orifice diameter is generally
kept as 0.5 times the diameter of
pipe, but it may vary from 0.4 to 0.8
times the pipe diameter.
11.
Orifice meter
• Adifferential manometer is connected at section (1), which
is at a distance of about 1.5-2.0 times the pipe diameter
upstream from the orifice plate, and at section (2) , which is
at a distance of about half the diameter of the orifice on the
downstream side from the orifice plate.
• Let p1 = pressure at section (1)
v1 = velocity at section (1)
a1 = area of pipe at section (1)
And, p2, v2, a2 are the
corresponding values at section (2)
Applying Bernoulli’s equation at
sections (1) and (2), we get
COMPARISON BETWEEN VENTURIMETER
ANDORIFICEMETER
Venturimeter
• It has tapered structure which
causes a gradual change in fluid
velocity.
• Pressure loss is less and its
coefficient of discharge is high.
• Expensive due to tapered
structure of the pipe.
• Suitable for fluids with high solid
content.
• The turn down ratio is about 10:1.
Orificemeter
• There is a sudden change in
fluid velocity because of the flat
flanges.
• Pressure loss is more and its
coefficient of discharge is low.
• Cheaper due to simple structure
of the pipe.
• Suitable for clean fluids.
• The turn down ratio is below 5:1.