Flow measurement pdf

Flow Measurements
Types of flow encountered:
• Clean or dirty
• Wet or dry
• Hazardous/corrosive or safe
• Single or multi phase
• Laminar of turbulent
• Varying pressure
Contents provided in this presentation are for reference purpose & the detailed theory to be read/written from respective text book/Class Notes
• Varying pressure
• Varying temperature
• Flow rates from least to highest
Types of flow measurements:
A. Primary or quantity meters
B. Positive displacement meters
C. Secondary of rate meters
D. Special methods

Flow Measurements
A. Primary or quantity meters:
Signifies the amount of fluid in terms of mass or volume
that flows past a given point in a definite period of time.
• Simple
• Economical
• Accurate
• Routinely used in the calibration of other flow measuring
devices
devices
1. Volumetric method:
Fluid flowing in the flow meter is diverted into a tank of
known volume. When the tank is completely filled, then
the known volume is compared with the integrated,
volumetric quantity registered by the flow meter under
test.

Flow Measurements
2. Gravimetric method:
Fluid flowing in the flow meter is diverted into a vessel
which can be weighted either continuously or in the
vessel after a pre-determined time. The weight of the
liquid collected is compared with the gravimetric quantity
registered by the flow meter under test.
B. Positive Displacement Meters:
Liquid flows through a meter and moves the measuring
Liquid flows through a meter and moves the measuring
element that seals the measuring chamber into a series of
measuring compartments each holding a definite volume.
Each element is successively filled from the flow at the
inlet and emptied at the outlet of the meter. In other
words these meters chop the flow into number of pieces
of known size and then count the number of pieces.

Flow Measurements
Features:
• Widely used in low flow rate metering applications where
high accuracy & repeatability are required.
• Easy to install
• Moderate cost
• Due to moving parts involved, wear of the components may
alter the accuracy.
• Suitable to clean fluids only.
• Suitable to clean fluids only.
• These devices are flow totalizes and generally and do not
give the instantaneous rate of flow.
• Cause pressure loss in the fluid system whose flow is being
metered.

Flow Measurements
1. Nutating Disc Meters:

Flow Measurements
Working:
• Liquid enters the left side of the meter, alternately above &
below the disc, forcing it to rock in a circular path while
rotating about its own axis.
• A small spindle attached to the sphere traces a circular path
and is used to drive the counter, which can be calibrated in
terms of liquid discharge.
Features:
Features:
• Simple & rugged construction
• Low pressure drop
• Low cost
• High accuracy of the order of ±1%.
• Widely used as a domestic water meter

Flow Measurements
2. Sliding Vane Type Meters:

Flow Measurements
Working:
• Liquid entering at inlet revolves the rotor and the vanes
around cam causing the vanes to move radially.
• Vane nearest to the inlet port begins to move outwards &
becomes fully extended at point A. While vane ahead at
point B is already fully extended, so a measuring chamber
of known volume is formed.
• A continuous series of chambers at the rate of four per
• A continuous series of chambers at the rate of four per
revolution are formed.
Features:
• Low pressure drop
• High accuracy of the order of ±0.2% of measured values.
• Can be used as a positive displacement pump which can
cause the flow and measure it simultaneously.

Flow Measurements
3. Lobed Impeller Meters:

Flow Measurements
Working:
• The incoming fluid is trapped between the two rotors and is
conveyed to outlet as a result of the rotor rotations.
• For every rotation of each rotor, the swept volume
corresponding to twice the area A is passed through meter.
• Number of revolutions of the rotor gives and indication of
volumetric flow.
• Rotation of lobed impellers can be monitored by magnetic
• Rotation of lobed impellers can be monitored by magnetic
or photo-electric pick up.
Features:
• Available for pressures up to 60 atm and flow range 10 to
10,000 m3/hr.
• High accuracy of the order of ±1% of rated capacity.
• Low pressure drop of the order of 50 mm of Hg.
• Relatively expensive.
• Applicable to clean fluids like gas metering.

Flow Measurements
C. Secondary or Rate Meters:
• Also termed as inferential type of flow measuring devices.
• They do not measure flow directly but instead measure
another physical quantity which is related to flow.
• Two categories:
Flow rate meters
Velocity meters or Anemometers

Flow Measurements
1. Variable Head Meters:
Features:
• Generally termed as obstruction type flow meters.
• The main forms of obstructions are: Venturi, orifice plate
and nozzle.
• The position of minimum pressure is located slightly
downstream from the restriction at a point where the
downstream from the restriction at a point where the
stream is narrowest and is called vena- contracta.
• Beyond this point the pressure the pressure again rises but
does not return to upstream value and thus there is
permanent pressure loss.
• No moving parts & so require no maintenance practically.
• Major disadvantage is square root relationship between
flow and head.
• Not suitable for flow below 20% of rated meter capacity.

Flow Measurements
a) Venturi Meter:

Flow Measurements
b) Orifice Meter:

Flow Measurements
c) Nozzle Meter:

Flow Measurements
Eqhg
AA
AA
solvingBy
Eqh
EqslliFromBernou
Eq
General
4.2Q:3&2Eq.1,
3.
g
p-p
:manometeratprdiffThe
2.
2
V
p
2
V
p:Eq.'
1.VAVAQ:dischargeofRate
:flowofrateforexpression
2
2
2
1
21
ideal
21
2
2
2
2
1
1
2211
∆
−
=
∆=
+=+
==
KK
KK
KK
KK
ρ
ρρ
g
AA
AA
EqhK
Eqhg
AA
AA
tCoefficien
practiceInactual
2KWhere
6.CQOr
5.2CQ
dischargeof
Q
Q
C
:soflow,actualthanmorealwaysisQ
2
2
2
1
21
dactual
2
2
2
1
21
dactual
ideal
actual
d
ideal
21
−
=
∆=
∆
−
=∴
==
KK
KK

Flow Measurements
Coefficient of discharge depends on:
• Type of flow
• Obstruction type configuration
• Reynolds number
Venturimeter Features:
• Best accuracy
• Least head loss as compared to orifice & nozzle meters
• Least head loss as compared to orifice & nozzle meters
• Due to low value of losses coefficient of discharge is high
• Can be used with dirty fluids also
• Relatively expensive
• Occupies substantial space

Flow Measurements
Nozzle Flow meter Features:
• Offers all the advantages of venturimeter but to a lesser
extent
• Occupies less space
• Nozzle is difficult to install and the installation is limited to
small to moderate pipe sizes
Orifice Flow meter Features:
Orifice Flow meter Features:
• Simple geometry, so cost is low
• Easy to install
• Takes almost no space
• Susceptible to inaccuracies due to erosion, corrosion,
clogging etc.
• Suffers from a head loss of the order of 30-40%

Flow Measurements2. Variable Area Meters: Features:
• In variable area meters the
area of restriction can be
altered to maintain the steady
pressure difference.
• Common variable area meter
is rotameter.
• The float will rise to a point in
the tube where the drag force
the tube where the drag force
(Up) & Buoyant force (Up) is
balance by the weight of the
float.
• The position of the float in
the tube is taken as an
indication of flow rate.
• It is also called as variable
area flow meter.

Flow Measurements
)p-p()(
floatoffacesupward&downwardat thepressuresthearep&p
floattheofvolumetheisV
lyrespectivefluidflowingandfloattheofdensitiestheare&Where
7.)(
A
V
)p-p(
gVgV)p-(pA
FFF
:isfloattheofforequationbalanceforceThe
ud
f
fff
fff
f
f
ud
fffffudf
weightbuoyancydrag
AAA
Eqg
Or
KK
−
−=∴
=+
=+
ρρ
ρρ
ρρ
10.)(Q:Then,1
)(
If
9.
)(
A
V
2
)(
1
)(
CQ:8&Eq.7From
float&tubeebetween thareaannularmintheis)(
levelfloatattubetheofareatheisA
8.
)p-p(
2
)(
)(
CQ:earlierEq.6From
actual
ff
fff
f
f
2
2dactual
t
ff
ud
22dactual
EqAAK
A
AA
Eqg
A
AA
AA
AA
Where
Eq
g
g
AAA
AAA
ft
t
ft
t
ft
ft
ft
ftt
ftt
KK
KK
KK
−=<<
−
−
−
−
−
=
−
−−
−
=
ρ
ρρ
ρ

Flow Measurements
inletatdiaisandinletrespect toithposition wfloattheisyWhere
11.tan
24
)tan(
4
thensmall),veryis(WhichistaperofangletheIf
constantrotametertheisKWhere
2
2
D
EqyDDAOr
yDA
i
iit
it
KK+=
+=
θ
ππ
θ
π
θ
scale.linearaonfloattheofreadingdirectagivesrotameterThus
float&rotametertheofshapeon thedependingconstantsareK&Where
13.Q
12.)
4
(tan
2
Q
)tan
24
(Q
11&Eq.10From
21
21actual
2
actual
2
actual
K
EqKyK
EqADKyDK
AyDDK
fii
fii
KK
KK
+=
−+=
−+=
π
θ
π
θ
ππ

Flow Measurements
Rotameter Features:
• Rotameter tube is made of high strength borosilicate glass
to allow direct observation of the float position.
• Main advantage is that they give direct visual indication on
linear scale.
• Can be used for wide ranges (from 0.1 ml/min to several
hundred lpm)
hundred lpm)
• Accuracy is generally ±1% of max flow rate, but up to ±5%
of rated capacity for very cheaper units.
• Can handle wide variety of fluids including corrosive ones.
• The disadvantage is that it can only be mounted in vertical
direction.
• Can be subjected to oscillations in pulsating flows.

Flow Measurements
3. Variable Head & Variable Area flow Meters:

Flow Measurements
dyy2gLCQ
H,to0fromequationabovethegIntegratin
14.dyL2gyClayerthinthefromdischargeactualAnd
dyL2gylayerthintheofDischarge
2gyfluidoflayerofVelocity
:levelwatertheofsurfacetopthefromyofdepthaat
dythicknessfluidoflayeragconsiderin,correctionendhoutr weir witrectangulaaFor
H
wd
w
EqKK
=
=
=∴
=
∫
( )
[ ] ( ) 16.2g2.0LC
3
2
Q
sides.bothon0.1Hofcontactionend
toduelengthcrestactualthat thelessisweirtheoflengthcresteffectivepracticeIn
15.2gLC
3
2
Q
dyy2gLCQ
2
3
wdactual
2
3
wdactual
0
wdactual
EqHH
EqH
KK
KK
−=∴
=
= ∫

Flow Measurements
Weir type Flow meters Features:
• Variable head variable area flow meters.
( )
( ) 18.2g
2
tanC
15
8
Q
isr weirtriangulaofequationDischarge
17.2gLC
3
2
Q
:isweircipollettioraltrapezoidaforequationdischargetheSo,
shapeinezoidalweir trapthemakingbyofcaretakenisnscontractioendofeffectThe
2
5
dactual
2
3
wdactual
EqH
EqH
KK
KK
θ
=
=
• Variable head variable area flow meters.
• Principle: If a restriction of a specified shape and form is placed
in the path of the flow, a rise in upstream liquid level occurs
which is a function of the rate of flow through the restricted
section.
• Rectangular weir suitable for large flow while triangular weir is
used for smaller flows below 50l/s.
• Simple in construction, easy to install and accurate devices.
• Main disadvantage is their non-linear characteristics.

Flow Measurements
4. Linear Resistance Element flow Meters:

Flow Measurements
Features:
• Principle: Based on Hagen- Poiseuille equation for laminar flow.
Where Q is the flow rate, D is the inside diameter of the tube, L is
length of tube, µ is the coefficient of viscosity and is the
pressure drop along the length of tube.
• Used for very small flow rates of highly viscous flows.
( )21
4
128
pp
L
D
Q −=
µ
π
( )21 pp −
• Used for very small flow rates of highly viscous flows.
• Flow rate is directly proportional to pressure drop (Linear
characteristics)
• Main disadvantage is that metering element is subjected to
plugging if fluid is not clean.
• Relatively expensive.
• High pressure losses.

Flow Measurements
5. Pitot Static Tube:

Flow Measurements
Features:
• Principle: Variable head velocity measuring device.
• Consists of two concentrically arranged tubes bent at right
angle.
• Inner tube faces the flow impingement and hence measures
static and dynamic pressures while outer tube measures the
static pressure.
( )
pressure.staticis
andpressurestagnationisdensity,fluidisvelocity,flowisVWhere
2
2
:EqsBernoulli'By
flow,fluidssfrictionleandibleincompressl,dimensionaoneaFor
2
statstag
statstag
stagstat
pp
pp
V
pVp
ρ
ρ
ρρ
−
=∴
=+

Flow Measurements
Advantages of Pitot tube:
• Simple & low cost device
• No appreciable pressure loss
• Easy installation
• Useful in measuring flow velocities
Limitations of Pitot tube:
• Not suitable for measuring low velocities i.e. below 5 m/s
• Sensitive to misalignment of the probe with respect to free
• Sensitive to misalignment of the probe with respect to free
stream velocity.
• Not suitable for measuring highly fluctuating velocities.
• Not commonly used in industrial applications as numerous Pitot
tube traverses are required for velocity distribution data which is
quite tedious & time consuming.

Flow Measurements
6. Target Flow Meter:

Flow Measurements
Features:
• Principle: The drag force onto a suitably shaped body into a flow
stream can be a measure of the flow rate after suitable
calibration.
)m(insectioncrossofAreaA
dragoftCoefficienWhere
2
1
2
2
=
=
= ρ
d
dd
C
AgVCF
velocityFluidV
)kg/m(indensityFluid
)m(insectioncrossofAreaA
3
=
=
=
ρ
• Main advantage is its very good dynamic response.
• Overall accuracy is ±0.5%
• Applications: Highly viscous flows of tar, oils or slurries at high
pressures of the order of 100 bars.

Flow Measurements
7. Turbine Flow Meter:

Flow Measurements
Features:
• Principle: Turbine meters are inferential measurement devices
that measure a flow rate indirectly by using the natural kinetic
energy of the flow as it passes through the angled blades of the
turbine rotor. This causes the turbine to spin and as the blades
pass by a close pre positioned magnetic (Or other
technology)“pick up” coil. The resulting interruption of the coils
magnetic field by each blade results in a pulse being produced.
magnetic field by each blade results in a pulse being produced.
The frequency of this pulse is directly proportional to the point
velocity reading it is taking. From this point velocity and cross
sectional area of the pipe a rough volumetric flow rate can be
calculated.
Q = k X n
Where k = Constant for any given meter
n = rotor angular velocity

Flow Measurements
Features:
• These meters have linear relationship between volume flow rate
and the angular velocity of the rotor.
• Accuracy of instruments is ±1%
• Commercially available for flow rates ranging from 0.5 to 150000
LPM (for liquids) and from 5 to 100000 LPM (For air).
• Bearing maintenance is a problem and accuracy drops off greatly
• Bearing maintenance is a problem and accuracy drops off greatly
at low flow rates.

Flow Measurements
8. Vortex Shedding Flow Meter:

Flow Measurements
Features:
• Principle: If a bluff body or an obstruction is placed in a fluid
stream, vortices are shed alternately on each side of the bluff
body. The vortex shedding frequency of the bluff body is a
measure of the average flow velocity of the fluid flow.
• Strouhal number S governs the operation of vortex shedding
flow meter:
flow meter:
numberStrouhalS
flowtheofvelocityAverageV
bodyblufftheoflengthsticcharacteriorDiameterD
frequencysheddingVortexWhere
=
=
=
=
=
s
s
f
V
Df
S

Flow Measurements
• h= height of the bluff body, generally the ratio of height to the
pipe dia should not be less than 0.2
• L=Length of shedder taken approx 1.3h
• Value of Strouhal number S for triangular wedge shaped body
remains nearly constant value of 0.88±0.01 over a wide range of
Reynolds number.
1.136D)(V
88.0
s
s
for
Df
V
=
=∴
)1.136D(
4
Q
sheddertheofdownstreamflowofVelocity
sheddertheofupstreamflowofVelocityWhere
44
Q
:asevaluatedbecanmeterflowvortexin therateFlow
1.136D)(V
2
22
s
d
u
du
s
fhDD
V
V
VhDDVD
for






−=∴
=
=






−==
=
π
ππ
Measurement of vortex shedding frequency is done by monitoring the alternating
strain signals from the strain gauge.

Flow Measurements
Advantages of Vortex shedding Flow meter:
• No moving parts and causes very low pressure loss
• Linear characteristics with respect to the shedding frequency
• Calibration constant is same for all fluids
• Calibration constant is not affected by the changes in the fluid
properties.
• Accuracy is of the order of ±0.5%
• Accuracy is of the order of ±0.5%
• Main disadvantage is inability to give accurate results for
Reynolds number <103 and > 107

Flow Measurements
D. Special Methods
1. Ultrasonic Flow Meters:
Travel time difference
method (Single Transmitter-
Receiver System)
Fig.1
Travel time difference
method (Twin Transmitter-
Receiver System)
Fig.2

Flow Measurements
Oscillating Loop Method
Fig.3
fluidin thesoundof
receiver&ansmitterbetween trdistanceWhere
t
:bygivenisreceivertheto
ertransmittthefrompulsetheoftimetransit tthevelocity,flowzeroWith
0
0
VelocityV
l
V
l
s
s
=
=
=

Flow Measurements
( )
1
V
t
,VgConsiderin
1.
V
V
or t
V
t
:becomestimetransit tthe,Vcitywith velofluidmovingaIn
s
22
s
s
s
s
V
Vl
V
Eq
V
Vl
V
l






−=
>>>
−
−
=
+
=
KK
)(as3.tor
-tt
Eq.2From
2.1or t
1
V
t
02
00
0
s
ss
s
s
s
V
l
tEq
V
lV
V
V
tt
Eq
V
V
t
V
==∆






==∆






−=




−=
KK
KK

Flow Measurements
VV
-tt
:directionfloweagainst thimetransit tistanddirectionflow
inimetransit ttheistIfprovided.is(Fig.2)systemreceiver
-ertransmittofsetadditionalanHence(Fig.1),tarrangemen
presentin theprovidednotisoftmeasurementheSince
ss
12
2
1
0
V
l
V
l
tThen
t
+
−
−
==∆
4.
V
2
t
VSince
V
2
tor
VV
2
s
s
22
s
ss
Eq
lV
V
V
lV
VV
KK=∆∴
>>>
−
=∆
+−

Flow Measurements
time.acousticaltheequalsperiodtimepath whoseeachinpulsesof
trainageneratesThission.retransmisforrtransduceingtransmitttheback to
fedouslyinstantaneandamplifiedispulseThis.tafter timeRtransducer
receivingby thereceivedisandTrtransduceingtransmittby theemitted
ispulseamethod,In thismethod.differencefrequencythecalledalso
(Fig.3),systemloopgoscillatintheistechniquein thisapproachAnother
.Vtodependentstronglyisconstantncalibratioehowever th
,VconstantforVinlinearisttoalproportionsignaloutputtheThus
11
1
s
s∆
5.
2
or
VV
-
V1
V1
:areflowfluideagainst thandalongsfrequencierepetitionThe
ss
12
s
2
2
s
1
1
Eq
l
V
f
l
V
l
V
fffThen
l
V
t
f
l
V
t
f
KK=∆
−
−
+
==∆
−
==
+
==

Flow Measurements
Advantages of Ultrasonic Flow meter:
• Negligible resistance to metering fluid system
• Reasonably good Accuracy of the order of ±2%
• Is suitable for both liquids and gases
• Output read out can easily be either analog or digital
• Has a linear relationship between the velocity and output

Flow Measurements
2. Electromagnetic Flow Meters:

Flow Measurements
Features:
• Suitable for electrically conducting fluids
• Principle: Faraday’s law of electromagnetic induction for solid
conductors. It states that whenever a conductor cuts lines of
magnetic field, an induced emf is generated and the magnitude
of this emf is proportional to the rate at which these lines are
cut and the emf is perpendicular to the plane of conductor and
magnetic field. The direction of induced emf is given by the
magnetic field. The direction of induced emf is given by the
Fleming’s right hand rule.
cm/s)(inconductortheofVelocityv
cm)(inconductiontheof
)s/cm-V(indensityfluxMagneticB
voltageInducedWhere
Volts10X
2
0
8
0
=
=
=
=
= −
Lengthl
E
BlvE

Flow Measurements
.Eemfinducedthetoalproportiondirectlyisrateflowthat theshowsThis
Volts10X
d
4B
Qor
4
Q
:asgivenpipeiscircularfor therateflowVolume
0
8
2
−
=
=
Q
vd
π
π
• This type of flow meter causes no obstruction to the flow
line of metered fluid
line of metered fluid
• Device is quite accurate and has wider range with good
transient response
• Can be used for dirty, corrosive, cement slurries etc flows
• These meters are expensive and their use is limited to fluids
having conductivity at least of the order of 1 X 10-6

Flow Measurements
3. Hot Wire Anemometer:

Flow Measurements
Features:
• Used for measuring mean and fluctuating velocities
• Flow sensing element is a Platinum- Tungsten wire
• Principle: When a heated probe is introduced in the fluid
stream, it tends to get cooled by the instantaneous velocity and
consequently there is a decrease in its resistance. If the same is
connected by a Wheatstone bridge then the instrument
response is the direct measure of the flow velocity and hence
response is the direct measure of the flow velocity and hence
the flow.
• The velocity measurement is done in two ways:
1. Constant current method: In this method, the sensing element
is feed constant current, the knowledge of this current and the
resistance of the wire defines the power being fed to the wire,
which is a function of the flow velocity. This method can be
used at higher frequencies and relatively small signals.

Flow Measurements
2. Constant resistance or constant temperature method: In this
method, the current to the hot wire is continuously adjusted
by means of a suitable servo system to maintain the resistance
of wire and hence the wire temperature at a contant value
throughout the range of hot wire operation. The current or
voltage is then the measure of the heat transfer rates and
hence the fluid velocity.
hot wireofDiaD
fluidtheofviscosityoftCoefficien
streamfluidtheofvelocityv
fluidtheofDensity
hot wireoftyconductiviThermalk
ferheat transoftcoefficienfilmConvectivehWhere
1.5.030.0
:lawsKing'onbasedisoperationhot wiretheofequationgoverningbasicThe
2
1
=
=
=
=
=
=






+=
µ
ρ
µ
ρ
Eq
VD
k
hD
KK

Flow Measurements
:followsaswrittenbealsocanEq.1
hot wireofDiaD
fluidtheofviscosityoftCoefficien
streamfluidtheofvelocityv
fluidtheofDensity
hot wireoftyconductiviThermalk
ferheat transoftcoefficienfilmConvectivehWhere
1.5.030.0
:lawsKing'onbasedisoperationhot wiretheofequationgoverningbasicThe
2
1
=
=
=
=
=
=






+= Eq
VD
k
hD
KK
µ
ρ
µ
ρ
( )
fluidflowingtheofeTemperaturT
retemperatuHot wireT
areaferHeat transA
powerthermaltoelectricalfromfactorK
wiretheofResistanceR
hot wirein theflowingCurrentIWhere
3.
:hot wireofconditionmequilibriuUnder the
2.
:followsaswrittenbealsocanEq.1
f
w
c
w
2
21
=
=
=
=
=
=
=
+=
Conversion
Eq-TThAKRI
EqVcch
fwcw KK
KK

Flow Measurements
( )( )
( )
( )
theandconstantisfactortheoperation,resistanceconstantFor
6.
RR
:5&Eq.4
5.RR
material.Tungsten-Platinumfor thedifferenceetemperatur
thetoalproportiondirectlyistwtotffromresistancein
4.:3&Eq.2From
21
fw
3
2
3fw
21
2
R
EqVcc
AK
CRI
From
Eq-TTC
Change
EqVcc-TTAKRI
w
c
w
fw
fwcw
KK
KK
KK
+=
−
=−∴
+=
7.:eq.6from
I.to
alproportiondirectlyiswhichEwithreplacedbecanIcurrenthot wireofvalue
theandconstantis
RR
factortheoperation,resistanceconstantFor
21
2
fw
EqVBAE
Rw
KK+=∴
−

Flow Measurements
( ) 2
1
0
2
0
2
9.4
2
1
2
:getweating,Differentivelocity.zeroatemftheis
8.
:aswrittenbealsocan7Eq
EqEdE
V
BdV
dVVBEdE
EWhere
EqVBEE
=
=∴
+=
−
KK
KK
2
0
2
2
0
2
2
0
2
4
isleveleturbulenctheHence
4
4:9&8eqFrom
EE
Ee
EE
EdE
V
dV
EdE
V
dV
V
EE
V
−
=
−
=
=
−

Flow Measurements
Advantages of hot wire anemometer:
• Negligible resistance/disturbance to metering fluid system
• Excellent accuracy of the order of ±0.1% in the measurement of
mean velocities and ±2% in the measurement of turbulence
levels
• Exhibits excellent dynamic characteristics
• Measuring range can be from very low velocities to supersonic
velocities
• Shown on next slide are the Typical forms of hot wire film
anemometer probes used for liquid flows

Flow Measurements

Flow Measurements
4. Laser Doppler Anemometer:

Flow Measurements
Features:
• It is an optical type of velocity meter
• Principle: Operating principle of this device is based on the
Doppler shift in frequency of the light scattered by an object
moving relative to the radiating source. The technique basically
consists of focusing laser beams at the point in the fluid where
the velocity is to be measured. At this focal point, the laser light
scattered from the fluid or fluid particles entrained in the fluid is
scattered from the fluid or fluid particles entrained in the fluid is
sensed by a photo-detector. Signal processing of the photo-
detector output yields the magnitude of Doppler frequency shift
which is directly proportional to the instantaneous velocity of
the flow.
2
sin
2 θ
λ
v
f =∆
NOTE: Refer the detailed theory of Laser Doppler Anemometer from text book.

Flow measurement pdf

Recommended

Recommended

More Related Content

What's hot

What's hot (20)

Viewers also liked

Viewers also liked (7)

Similar to Flow measurement pdf

Similar to Flow measurement pdf (20)

Recently uploaded

Recently uploaded (20)

Flow measurement pdf