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8/18/2019 Volf Low Measurements
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Volume Flow MeasurementsVolume Flow Measurements
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Obstruction MetersObstruction Meters
Orifce Meters
Venturi Meters
Flow Nozzles
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Flow through a NozzleFlow through a Nozzle
2211
21
222111
21
vAvA
ibleincompressvAvA
Avmmm
=ρ=ρ
ρ=ρ
ρ==
1
1
1
1
v
A
mρ
2
2
2
2
v
A
m
ρ
Basic Equations:
a.) Continuity:
mass in = mass out
b.) Bernoulli’s Eqn.
Total pressure is
constant throughout
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pressuredynamicv
2
1
pressuretotalP pressurestaticP
PPv2
1Pv
2
1
Pv2
1
.constessurePr TotalPBernoulli
2
0
02
2
221
2
11
2
0
=ρ
==
=+ρ=+ρ
+ρ=
==
Flow through a NozzleFlow through a Nozzle
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ρ∆
−
=
ρ∆
−
==
ρ∆
−
=
P2
A
A1
1YCAQ
FlowaleFor
!dealP2
A
A1
1AvAQ
ateFlow
P2
A
A1
1v
2
1
2
2
2
1
2
222
2
1
2
2
Flow through a NozzleFlow through a Nozzle
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∆P21
2
1
22
2
2
2
2
1
21
2
22
2
11
2
2221
12
1
2
1
2
1
2
1
2
1
ρ ρ
ρ
ρ ρ
ρ ρ
=
−=
−=
−=−=∆
when
A
Av
v A
Av
vv P P P
Flow through a NozzleFlow through a Nozzle
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Y " Compressibility Factor
"1 #or incompressible #low
or w$en ∆P%% Pabs
C" &isc$ar'e Coe##icient
"#(e) and
nature o# speci#ic #low meter
∆P
Flow through a NozzleFlow through a Nozzle
P
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Flow through a Venturi Meter Flow through a Venturi Meter
!n a venturi* 0.+, % C % 0.+-
Advanta'e
Pressure recovery
/ses little power
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Flow through a Venturi Meter Flow through a Venturi Meter
C
R e
2 10,
µ
ρ= 11
vd
e
0.+-
Based upon t$e conditions in t$e pipe
approac$in' t$e meter
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Back to the NozzleBack to the NozzleP1 P2
P
P1
P2
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$orter and c$eaper t$an venturi
But lar'er pressure drop.
T$us* more power lost in operatin'.
The Nozzle Flowmeter The Nozzle Flowmeter
C
0.-
0.+-
10310,
e
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Flow Through an OrifceFlow Through an Orifce
Meter Meter
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Flow Through an OrifceFlow Through an Orifce
Meter Meter P
1P
2
P
P1
d &
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Flow Through an OrifceFlow Through an Orifce
Meter Meter
4C$eapest and implest4But bi''est pressure drop and power lost (C50. 4 0.6)
4ide 7ote
Pressure drop caused by #riction and turbulence o# s$ear
layer downstream o# vena contracta
CM
A
A
C =
−
2
1
21
1
0.
0.-,
β"d8&0.1 0.-
e
1009
,000
109
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:lbow Flowmeter
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;aminar
Flowmeter
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Pitot-Static TubesPitot-Static Tubes
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Rotameter !ariable-area-Rotameter !ariable-area-
"owmeter "owmeter
Force balance Drag Force
Gravity
Buoyancy
(usually negligible)
cal
usecal use mm
ρ
ρ =
&erived on net
slide
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D
MgA
D
Mg Am
D
Mg V
Mg V
D F
V Am
2
2
22
2
2
ρ ρ
ρ
ρ
ρ
ρ
==
=
==
=
For a #ied 4position* A is #ied. T$en
cal
usecal use
cal use
mm
mm
ρ
ρ
ρ ρ
=
=
otameter
:
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Turbine Flow MetersTurbine Flow Meters
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=orte meters operate on t$e principle t$at w$en a non4streamlined
ob>ect is placed in t$e middle o# a #low stream* vortices are s$ed
alternately downstream o# t$e ob>ect. T$e #re
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Magnetic "owmeter Magnetic "owmeter
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Based upon Faraday’s a!
T$e #luid is t$e conductor* must be electrically conductive.
:"B&=104-
:"volta'e* volts
B"ma'netic #lu density* 'auss
&" len't$ o# t$e conductor* cm
="velocity o# t$e conductor* cm8sec
Magnetic "owmeter Magnetic "owmeter
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#oriolis Mass Flow Meter #oriolis Mass Flow Meter
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#oriolis Mass Flow Meter #oriolis Mass Flow Meter
=ibratin' Flow TubeFluid Force is eactin' to =ibration
o# Flow Tube
:nd =iew o# Flow Tube
$owin' Twist
Twist An'le
Twist An'le
Flow
Force
Flow Force
Flow
Flow
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#oriolis Mass Flow Meter #oriolis Mass Flow Meter
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Positive
&isplacement
?eters
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