SlideShare a Scribd company logo
3
Most read
8
Most read
16
Most read
VARIABLE HEAD METERS
 Guided By: Presented By : Shivang Bansal
Mr. Rahul Bhargava (0818CM141011)
Pitot tube :-
Working principle and construction :
The velocity distribution across a section can be obtained with help of a pitot
tube, which is one of the most accurate device for velocity measurement.
It consist of a glass tube in form of 90˚ bend of short length open at both of its
ends. It is placed in flow with its bent leg directed upstream so that a stagnation
point is created immediately in front of opening . The kinetic energy at this point
gets converted into potential energy causing the liquid to rise in vertical limb, to
a height equal to the stagnation pressure.
Applying Bernoulli's equation between stagnation point (s) & point(p) in
undistributed flow at the same horizontal plane, we get:
Po /W + v2 /2g = Ps /w
OR ho + v2/2g = hs
Po & Ps = pressure at point ‘P’ & point ‘S’
V = free flow velocity
ΔH = dynamic pressure
The height of liquid rise indicates stagnant pressure head . it can also be
measured with the help of piezometer.
Advantage:-
1. Negligible loss of heat when pitot tube is inserted in the
pipe.
2. Uses costly as compared to venturimeter or orificemeter.
3. Easy to install & remove from the pipeline.
Disadvantages:-
1. Poor accuracy.
2. Unsuitable for dirty or sticky liquids.
3. Requires high flow velocity of about 15m/s to produce
measureable heats.
4. Sensitive to upstream disturbance to reynolds number
changes and to dimension errors.
5. Cannot be used for industrial application which require
an instant readout.
Orificemeter:-
Is an opening usually round located in the side wall of tank or reservoir
for measuring flow of liquid. The main feature is that most of the
potential energy of liquid is converted into kinetic energy of free jet
issuing through the orifice.
Also used for flow measurement in a pipe.
It consist of a flat circular plate having a circular sharp edged hole
concentric with the pipe. The diameter of orifice may vary from 0.4-0.8
times the diameter of pipe but its value is generally chosen is 0.5.
A differential manometer is connected at section 1 which is at a distance to
1.5-2 times the pipe diameter upstream from the orifice plate , and at section
2 which is at a distance of about half the diameter of orifice from orifice
plate from downstream side.
Jet coming out of orifice plate gradually expands from vena contracta to fill
the pipe.
Figure shows the location of vena contracta point. A part of kinetic energy
of the jet is converted into point using eddy currents causing dissipation of
energy and loss of head.
Disadvantages:-
1. Low coefficient of discharge.
2. Poor pressure recovery.
3. Susceptible to inaccuracies resulting from erosion, corrosion and
sealing.
4. Lower physical strength orifices are likely to be damaged by pressure
transients.
1. Low initial cost.
2. Easy to install.
3. Simple and less expensive maintenance as compared with
venturimeter.
4. Requires less spaces as compared to a venturimeter.
5. Can be used in wide range of pipe sizes(1.25-1.50cm)
Advantages:-
Venturimeter:-
Working :
 It consist of a short converging conical tube which has a total included
angle of 21 ± 1° leading to a cylindrical portion of short length, known
as throat.
 It is followed by diverging section known as diffuser having a total
included angle 5° to 7° .
 The pressure difference measure between the entry section 1 and the
throat section 2, usually by means of a U-tube manometer.
 The axis of Venturimeter may be horizontal or inclined or vertical.
 Area of flow in divergent section is increased gradually to avoid
separation of flow and reduce friction losses.
 The value of coefficient of discharge varies from 0.95 to 0.99.
Disadvantages of Venturimeter :
 Highly expensive.
 Occupies considerable space.
 Cannot be altered for measuring pressure beyond a
maximum velocity.
Difference between orifice meter and
venturi meter :
 The orifice plate can easily be changed to accomodate widely different
flow rates, whereas the throat diameter of a venturi is fixed, so that its
range of flow rates is circumscribed by the practical limits of Dp.
 The orifice meter has a large permanent loss of pressure because of the
presence of eddies on the downstream side of the orifice-plate; the
shape of the venturi meter prevents the formation os these eddies and
greatly reduces the permanent loss.
 The orifice is cheap and easy to install. The venturi meter is expensive,
as it must be carefully proportioned and fabricated. A home made
orifice is often entirely satisfactory, whereas a venturi meter is
practically always purchased from an instrument dealer.
 On the other hand, the head lost in the orifice for the same conditions
as in the venturi is many times greater. The power lost is proportionally
greater, and, when an orifice is inserted in a line carrying fluid
continuously over long periods of time, the cost of the power may be
out of all proportion to the saving in first cost. Orifices are therefore
best used for testing purposes or other cases where the power lost is not
a factor, as in steam lines.
 However, in spite of considerations of power loss, orifices are widely
used, partly because of their greater flexibility, because installing a new
orifice plate with a different opening is a simpler matter. The venturi
meter can not be so altered. Venturi meters are used only for
permanent installations.
 It should be noted that for a given pipe diameter and a given diameter
of orifice opening or venturi throat, the reading of the venturi meter for
a given velocity is to the reading of the orifice as (0.61/0.98)2, or
1:2.58.(i.e. orifice meter will show higher manometer reading for a given
velocity than venturi meter).
Weir :
 A weir basically an obstruction in the flow path in an open channel.
 The weir will cause an increase in the water depth as the water flows
over the weir.
 In general, the greater the flow rate, the greater will be the increase in
depth of flow. The height of water above the top of the weir is the
measurement usually used to correlate with flow rate.
Drawbacks of Weirs :
 A weir will artificially reduce the upstream water velocity,
which can lead to an increase in siltation.
 Weirs can also have an effect on local fauna.
 Even though the water around weirs can often appear
relatively calm, they can be extremely dangerous places to
boat, swim or wade, as the circulation patterns on the
downstream side – typically called a HYDRAULIC JUMP –
can submerge a person indefinitely.
 This phenomenon is so well known to persons who spend
time on rivers that they even have a rueful name for weirs :
“ Drowning Machines”.
 The weir can become a point where garbage and other
debits accumulate.
Notches :
 A notches is defined as an opening in the side of a vessel or tank
in such a manner that the liquid surface in the tank.
 A notch is generally made of metallic plate.
 It is used for measuring the discharge rate of a liquid from a
small channel or tank.
Flumes :
 A flume is a man made channel for water, in the form of an open
declined gravity channel whose walls are raised above the surrounding
terrain, in contrast to a trench or ditch.
 Some varieties of flumes are used in measuring water flow of a larger
channel.
THANK YOU

More Related Content

PPTX
Reciprocating Pump
PPTX
presentation on heat exchanger
PPTX
Transmitter By MItesh Kumar
PPTX
Heat exchangers and types
PDF
ROTAMETER: ITS CONSTRUCTION AND WORKING
PPT
Level measurement
PDF
Steam ejector working principle
PDF
Heat Exchangers
Reciprocating Pump
presentation on heat exchanger
Transmitter By MItesh Kumar
Heat exchangers and types
ROTAMETER: ITS CONSTRUCTION AND WORKING
Level measurement
Steam ejector working principle
Heat Exchangers

What's hot (20)

PPTX
Flow measurement
PPTX
Gas turbine cycle (open and closed gas turbine cycle)
PPT
Boilers and its types & components
PPTX
boiler & classification of boiler
PPT
Steam boiler
PPTX
Control valves
PPT
Pressure measurement
PPTX
Vapour absorption system
PPT
various flow meter
PDF
Boiler Mountings and Accessories.pdf
PPT
Flow measurement
PPTX
Fans and blower
PPTX
Classification of heat exchanger
PPTX
Refrigeration and air conditioning ppt
PPTX
Thermocouples
PPTX
Evaporators
PPTX
Bernoulli Equation
PPT
Industrial fan(ID FD Fans)
PPTX
Bourdon pressure gauge
Flow measurement
Gas turbine cycle (open and closed gas turbine cycle)
Boilers and its types & components
boiler & classification of boiler
Steam boiler
Control valves
Pressure measurement
Vapour absorption system
various flow meter
Boiler Mountings and Accessories.pdf
Flow measurement
Fans and blower
Classification of heat exchanger
Refrigeration and air conditioning ppt
Thermocouples
Evaporators
Bernoulli Equation
Industrial fan(ID FD Fans)
Bourdon pressure gauge
Ad

Viewers also liked (20)

PPTX
Venturimeter,Orificemeter,Notches & weirs,Pilot tubes
PPTX
Flow through orifice meter
PPT
flow through venturimeter
PPTX
PPTX
Venturimeter (FLUID MECHANICS)
PPTX
Venturimeter
PDF
[Oil & Gas White Paper] Gas Measurement and Analysis to Support Financials
PDF
Vortex flowmeter for gas, steam and liquids
PDF
The Global Development and future of Natural gas measurement_Jacob Freeke
DOC
Orificemeter
PPT
Gas measurement
PDF
Drager Gas Measurement & Gas Sampling - A Laboratory Behind Glass
PPTX
SEMINAR AGA REPORT NO 7
DOC
Unit 5 Fluid Mechanics
PPTX
Flow measurement & vibration
PDF
Flow of Fluids
PPT
9. fm 9 flow measurement co 4 adam
PDF
Comparison of Orifice, Venturi & Rota meter
PPT
7. fm 8 bernoulli co 2 adam edit
PPT
Material balance Equation
Venturimeter,Orificemeter,Notches & weirs,Pilot tubes
Flow through orifice meter
flow through venturimeter
Venturimeter (FLUID MECHANICS)
Venturimeter
[Oil & Gas White Paper] Gas Measurement and Analysis to Support Financials
Vortex flowmeter for gas, steam and liquids
The Global Development and future of Natural gas measurement_Jacob Freeke
Orificemeter
Gas measurement
Drager Gas Measurement & Gas Sampling - A Laboratory Behind Glass
SEMINAR AGA REPORT NO 7
Unit 5 Fluid Mechanics
Flow measurement & vibration
Flow of Fluids
9. fm 9 flow measurement co 4 adam
Comparison of Orifice, Venturi & Rota meter
7. fm 8 bernoulli co 2 adam edit
Material balance Equation
Ad

Similar to Variable Headmeter (20)

PDF
Flow measurement part II
PPTX
venturi and orifices meter
PPTX
Importance and Practical application of Fluid Mechanics sessional
PPTX
Flow Measurnment
PPTX
Flow measuring devices
PPTX
Ch. no. 4 flow measurement
PPTX
orifice meter and pitot tube
PPTX
Design Of Flow Meters
DOCX
Energy losses in Bends, loss coefficient related to velocity head.Pelton Whee...
PPTX
Pump principles
PPTX
orifice meter and its application_ppt
PPT
Flow-Measurement- it's definition , types, example ppt.ppt
PPTX
process instrumentation and control lecture 2
PPTX
lecture 2 of process instrumentaiton and control
PDF
INSTRUMENTATION IN EASY LANGUAGE.pdf
PDF
Flow measurement part III
PDF
Flow Measuring Device
PPTX
Flow sensors
PPTX
Flow measurement in industries
PPT
12 Flow measurement.ppt
Flow measurement part II
venturi and orifices meter
Importance and Practical application of Fluid Mechanics sessional
Flow Measurnment
Flow measuring devices
Ch. no. 4 flow measurement
orifice meter and pitot tube
Design Of Flow Meters
Energy losses in Bends, loss coefficient related to velocity head.Pelton Whee...
Pump principles
orifice meter and its application_ppt
Flow-Measurement- it's definition , types, example ppt.ppt
process instrumentation and control lecture 2
lecture 2 of process instrumentaiton and control
INSTRUMENTATION IN EASY LANGUAGE.pdf
Flow measurement part III
Flow Measuring Device
Flow sensors
Flow measurement in industries
12 Flow measurement.ppt

Recently uploaded (20)

PPTX
MET 305 2019 SCHEME MODULE 2 COMPLETE.pptx
PDF
737-MAX_SRG.pdf student reference guides
PDF
Mitigating Risks through Effective Management for Enhancing Organizational Pe...
PPTX
Infosys Presentation by1.Riyan Bagwan 2.Samadhan Naiknavare 3.Gaurav Shinde 4...
PPTX
Artificial Intelligence
PPTX
Construction Project Organization Group 2.pptx
PDF
III.4.1.2_The_Space_Environment.p pdffdf
PPTX
Internet of Things (IOT) - A guide to understanding
PDF
Embodied AI: Ushering in the Next Era of Intelligent Systems
DOCX
ASol_English-Language-Literature-Set-1-27-02-2023-converted.docx
PDF
Enhancing Cyber Defense Against Zero-Day Attacks using Ensemble Neural Networks
PDF
R24 SURVEYING LAB MANUAL for civil enggi
PPT
introduction to datamining and warehousing
PDF
keyrequirementskkkkkkkkkkkkkkkkkkkkkkkkkkkkkkkkkkkkk
PDF
PREDICTION OF DIABETES FROM ELECTRONIC HEALTH RECORDS
PPTX
Geodesy 1.pptx...............................................
PPT
Total quality management ppt for engineering students
PDF
Human-AI Collaboration: Balancing Agentic AI and Autonomy in Hybrid Systems
PDF
null (2) bgfbg bfgb bfgb fbfg bfbgf b.pdf
PPTX
Sustainable Sites - Green Building Construction
MET 305 2019 SCHEME MODULE 2 COMPLETE.pptx
737-MAX_SRG.pdf student reference guides
Mitigating Risks through Effective Management for Enhancing Organizational Pe...
Infosys Presentation by1.Riyan Bagwan 2.Samadhan Naiknavare 3.Gaurav Shinde 4...
Artificial Intelligence
Construction Project Organization Group 2.pptx
III.4.1.2_The_Space_Environment.p pdffdf
Internet of Things (IOT) - A guide to understanding
Embodied AI: Ushering in the Next Era of Intelligent Systems
ASol_English-Language-Literature-Set-1-27-02-2023-converted.docx
Enhancing Cyber Defense Against Zero-Day Attacks using Ensemble Neural Networks
R24 SURVEYING LAB MANUAL for civil enggi
introduction to datamining and warehousing
keyrequirementskkkkkkkkkkkkkkkkkkkkkkkkkkkkkkkkkkkkk
PREDICTION OF DIABETES FROM ELECTRONIC HEALTH RECORDS
Geodesy 1.pptx...............................................
Total quality management ppt for engineering students
Human-AI Collaboration: Balancing Agentic AI and Autonomy in Hybrid Systems
null (2) bgfbg bfgb bfgb fbfg bfbgf b.pdf
Sustainable Sites - Green Building Construction

Variable Headmeter

  • 1. VARIABLE HEAD METERS  Guided By: Presented By : Shivang Bansal Mr. Rahul Bhargava (0818CM141011)
  • 3. Working principle and construction : The velocity distribution across a section can be obtained with help of a pitot tube, which is one of the most accurate device for velocity measurement. It consist of a glass tube in form of 90˚ bend of short length open at both of its ends. It is placed in flow with its bent leg directed upstream so that a stagnation point is created immediately in front of opening . The kinetic energy at this point gets converted into potential energy causing the liquid to rise in vertical limb, to a height equal to the stagnation pressure. Applying Bernoulli's equation between stagnation point (s) & point(p) in undistributed flow at the same horizontal plane, we get: Po /W + v2 /2g = Ps /w OR ho + v2/2g = hs Po & Ps = pressure at point ‘P’ & point ‘S’ V = free flow velocity ΔH = dynamic pressure The height of liquid rise indicates stagnant pressure head . it can also be measured with the help of piezometer.
  • 4. Advantage:- 1. Negligible loss of heat when pitot tube is inserted in the pipe. 2. Uses costly as compared to venturimeter or orificemeter. 3. Easy to install & remove from the pipeline. Disadvantages:- 1. Poor accuracy. 2. Unsuitable for dirty or sticky liquids. 3. Requires high flow velocity of about 15m/s to produce measureable heats. 4. Sensitive to upstream disturbance to reynolds number changes and to dimension errors. 5. Cannot be used for industrial application which require an instant readout.
  • 5. Orificemeter:- Is an opening usually round located in the side wall of tank or reservoir for measuring flow of liquid. The main feature is that most of the potential energy of liquid is converted into kinetic energy of free jet issuing through the orifice. Also used for flow measurement in a pipe.
  • 6. It consist of a flat circular plate having a circular sharp edged hole concentric with the pipe. The diameter of orifice may vary from 0.4-0.8 times the diameter of pipe but its value is generally chosen is 0.5. A differential manometer is connected at section 1 which is at a distance to 1.5-2 times the pipe diameter upstream from the orifice plate , and at section 2 which is at a distance of about half the diameter of orifice from orifice plate from downstream side. Jet coming out of orifice plate gradually expands from vena contracta to fill the pipe. Figure shows the location of vena contracta point. A part of kinetic energy of the jet is converted into point using eddy currents causing dissipation of energy and loss of head.
  • 7. Disadvantages:- 1. Low coefficient of discharge. 2. Poor pressure recovery. 3. Susceptible to inaccuracies resulting from erosion, corrosion and sealing. 4. Lower physical strength orifices are likely to be damaged by pressure transients. 1. Low initial cost. 2. Easy to install. 3. Simple and less expensive maintenance as compared with venturimeter. 4. Requires less spaces as compared to a venturimeter. 5. Can be used in wide range of pipe sizes(1.25-1.50cm) Advantages:-
  • 9. Working :  It consist of a short converging conical tube which has a total included angle of 21 ± 1° leading to a cylindrical portion of short length, known as throat.  It is followed by diverging section known as diffuser having a total included angle 5° to 7° .  The pressure difference measure between the entry section 1 and the throat section 2, usually by means of a U-tube manometer.  The axis of Venturimeter may be horizontal or inclined or vertical.  Area of flow in divergent section is increased gradually to avoid separation of flow and reduce friction losses.  The value of coefficient of discharge varies from 0.95 to 0.99.
  • 10. Disadvantages of Venturimeter :  Highly expensive.  Occupies considerable space.  Cannot be altered for measuring pressure beyond a maximum velocity.
  • 11. Difference between orifice meter and venturi meter :  The orifice plate can easily be changed to accomodate widely different flow rates, whereas the throat diameter of a venturi is fixed, so that its range of flow rates is circumscribed by the practical limits of Dp.  The orifice meter has a large permanent loss of pressure because of the presence of eddies on the downstream side of the orifice-plate; the shape of the venturi meter prevents the formation os these eddies and greatly reduces the permanent loss.  The orifice is cheap and easy to install. The venturi meter is expensive, as it must be carefully proportioned and fabricated. A home made orifice is often entirely satisfactory, whereas a venturi meter is practically always purchased from an instrument dealer.
  • 12.  On the other hand, the head lost in the orifice for the same conditions as in the venturi is many times greater. The power lost is proportionally greater, and, when an orifice is inserted in a line carrying fluid continuously over long periods of time, the cost of the power may be out of all proportion to the saving in first cost. Orifices are therefore best used for testing purposes or other cases where the power lost is not a factor, as in steam lines.  However, in spite of considerations of power loss, orifices are widely used, partly because of their greater flexibility, because installing a new orifice plate with a different opening is a simpler matter. The venturi meter can not be so altered. Venturi meters are used only for permanent installations.  It should be noted that for a given pipe diameter and a given diameter of orifice opening or venturi throat, the reading of the venturi meter for a given velocity is to the reading of the orifice as (0.61/0.98)2, or 1:2.58.(i.e. orifice meter will show higher manometer reading for a given velocity than venturi meter).
  • 13. Weir :  A weir basically an obstruction in the flow path in an open channel.  The weir will cause an increase in the water depth as the water flows over the weir.  In general, the greater the flow rate, the greater will be the increase in depth of flow. The height of water above the top of the weir is the measurement usually used to correlate with flow rate.
  • 14. Drawbacks of Weirs :  A weir will artificially reduce the upstream water velocity, which can lead to an increase in siltation.  Weirs can also have an effect on local fauna.  Even though the water around weirs can often appear relatively calm, they can be extremely dangerous places to boat, swim or wade, as the circulation patterns on the downstream side – typically called a HYDRAULIC JUMP – can submerge a person indefinitely.  This phenomenon is so well known to persons who spend time on rivers that they even have a rueful name for weirs : “ Drowning Machines”.  The weir can become a point where garbage and other debits accumulate.
  • 15. Notches :  A notches is defined as an opening in the side of a vessel or tank in such a manner that the liquid surface in the tank.  A notch is generally made of metallic plate.  It is used for measuring the discharge rate of a liquid from a small channel or tank.
  • 16. Flumes :  A flume is a man made channel for water, in the form of an open declined gravity channel whose walls are raised above the surrounding terrain, in contrast to a trench or ditch.  Some varieties of flumes are used in measuring water flow of a larger channel.