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VENTURIMETER
Aplication of Bernoulli’s Theorem
By:
Kundan Kumar
Asst. Professor
Department of Mechanical Engineering
HRIT Group of Institutions, Ghaziabad
©Copyright
Bernoulli's Theorem
Assumptions:
 no work or heat interaction between a
fluid element and the surrounding
takes place.
 The flow must be incompressible
 Friction by viscous forces has to be
negligible.
Bernoulli's Theorem
 This equation was developed first by
Daniel Bernoulli in 1738.
flow work
per unit
mass
kinetic
energy per
unit mass
potential
energy per
unit mass
Bernoulli's Theorem with Head Loss
Where, hf represents the frictional work done (the work
done against the fluid friction) per unit weight of a fluid
element while moving from a station 1 to 2 along a
streamline in the direction of flow.
Application of Bernoulli’s Law
 Orifice meter
 Venturi meter
 Venturimeter
 It is a device used for the
measurement of flow in a pipeline.
 Based on Principle of Bernoulli’s
theorem.
 It consist of 3 parts:
a) Converging Cone.
b) Short cylindrical throat.
c) Diverging cone.
 Venturimeter
Converging Cone:
 The function of converging cone is to
accelerate the flow and create pressure
difference between the inlet to converging
cone and the throat.
 Angle of Diverging cone is from 14˚ to 20˚.
 Venturimeter
Short Cylindrical throat:
 The function of throat is to stabilize the flow
and facilitate the provision of pressure
tapping.
 Diameter Ratio:
d/D = 0.4 to 0.7
Where, D= Diameter of Pipeline
d= Diameter of throat
 Venturimeter
Diverging cone:
 The function of diverging cone is to reduce
the velocity and increase the pressure to its
original value to the extent it is possible
practically.
 Angle of Diverging cone is from 5˚ to 7˚
 Venturimeter
Figure shows that a
venturimeter is inserted in
an inclined pipe line in a
vertical plane to measure
the flow rate through
the pipe.
Let us consider a steady, ideal and one
dimensional (along the axis of the venturi meter)
flow of fluid. Under this situation, the velocity and
pressure at any section will be uniform.
Let the velocity and pressure at the inlet (Sec.
1) are V1 and p1 respectively, while those at the
throat (Sec. 2) are V2 and p2.
 Venturimeter
Manometer
Throat
Diverging
Cone
Convergin
g Cone
 Venturimeter
 Now, applying Bernoulli’s equation between Section 1 and 2, we
get
where ρ is the density of fluid flowing through the venturimeter.
From continuity,
where A1 and A2 are the cross-sectional areas of the venturi meter at
its throat and inlet respectively. With the help of Eq. 1, Eq. 2 can be
written as
piezometric pressure heads respectively at
point 1 & 2 respectively.
 Venturimeter
Hence, the volume flow rate through the pipe is given by
This is the Equation of Discharge of flow through
venturimeter.
• Actual Discharge can be calculated by Multiplying the
Theoretical
Discharge with Coefficient of Discharge.
• The value of coefficient of discharge is ranging from 0.91 to
0.99,
depends upon the condition of flow and losses.
 Merit & Demerits
Merits:
 Recovery of Pressure is near original value
 Loss of energy is minimum.
Demerits:
 Its cost is High.
 Occupies more space than orifice meter.
 Uses & Applications
 Calculating flow rate of fluid in a tube.
 Setting the flow of gasoline in the ignition
system of a motor vehicle.
 In the field of medicine, has also designed
venturi meter is used to measure the rate of
blood flow in the arteries.
VENTURIMETER -Application of Bernoulli's Law

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VENTURIMETER -Application of Bernoulli's Law

  • 1. VENTURIMETER Aplication of Bernoulli’s Theorem By: Kundan Kumar Asst. Professor Department of Mechanical Engineering HRIT Group of Institutions, Ghaziabad ©Copyright
  • 2. Bernoulli's Theorem Assumptions:  no work or heat interaction between a fluid element and the surrounding takes place.  The flow must be incompressible  Friction by viscous forces has to be negligible.
  • 3. Bernoulli's Theorem  This equation was developed first by Daniel Bernoulli in 1738. flow work per unit mass kinetic energy per unit mass potential energy per unit mass
  • 4. Bernoulli's Theorem with Head Loss Where, hf represents the frictional work done (the work done against the fluid friction) per unit weight of a fluid element while moving from a station 1 to 2 along a streamline in the direction of flow.
  • 5. Application of Bernoulli’s Law  Orifice meter  Venturi meter
  • 6.  Venturimeter  It is a device used for the measurement of flow in a pipeline.  Based on Principle of Bernoulli’s theorem.  It consist of 3 parts: a) Converging Cone. b) Short cylindrical throat. c) Diverging cone.
  • 7.  Venturimeter Converging Cone:  The function of converging cone is to accelerate the flow and create pressure difference between the inlet to converging cone and the throat.  Angle of Diverging cone is from 14˚ to 20˚.
  • 8.  Venturimeter Short Cylindrical throat:  The function of throat is to stabilize the flow and facilitate the provision of pressure tapping.  Diameter Ratio: d/D = 0.4 to 0.7 Where, D= Diameter of Pipeline d= Diameter of throat
  • 9.  Venturimeter Diverging cone:  The function of diverging cone is to reduce the velocity and increase the pressure to its original value to the extent it is possible practically.  Angle of Diverging cone is from 5˚ to 7˚
  • 10.  Venturimeter Figure shows that a venturimeter is inserted in an inclined pipe line in a vertical plane to measure the flow rate through the pipe. Let us consider a steady, ideal and one dimensional (along the axis of the venturi meter) flow of fluid. Under this situation, the velocity and pressure at any section will be uniform. Let the velocity and pressure at the inlet (Sec. 1) are V1 and p1 respectively, while those at the throat (Sec. 2) are V2 and p2.
  • 12.  Venturimeter  Now, applying Bernoulli’s equation between Section 1 and 2, we get where ρ is the density of fluid flowing through the venturimeter. From continuity, where A1 and A2 are the cross-sectional areas of the venturi meter at its throat and inlet respectively. With the help of Eq. 1, Eq. 2 can be written as piezometric pressure heads respectively at point 1 & 2 respectively.
  • 13.  Venturimeter Hence, the volume flow rate through the pipe is given by This is the Equation of Discharge of flow through venturimeter. • Actual Discharge can be calculated by Multiplying the Theoretical Discharge with Coefficient of Discharge. • The value of coefficient of discharge is ranging from 0.91 to 0.99, depends upon the condition of flow and losses.
  • 14.  Merit & Demerits Merits:  Recovery of Pressure is near original value  Loss of energy is minimum. Demerits:  Its cost is High.  Occupies more space than orifice meter.
  • 15.  Uses & Applications  Calculating flow rate of fluid in a tube.  Setting the flow of gasoline in the ignition system of a motor vehicle.  In the field of medicine, has also designed venturi meter is used to measure the rate of blood flow in the arteries.