Chapter 15 Flow Measpurements
Transcript of Chapter 15 Flow Measpurements
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Chapter 15 Flow Measurements
Measuring flow rate is extremely important for many industrial
processes, and often is necessary in the lab also. The term flow rate is
ambiguous, we should specify whether we mean mass flow rate or
volume flow rate.
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Conservation of Mass
dmsys
dt m
inlet
mexit
(From Thermo)
tdV U
CS
CV
ndA 0 (From Fluids)
m UA
ndA U
A
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Volume Flow
If the density is constant, then this tells us that the volume flow is
fixed, orQin = Qout where
Q UA
ndA U A
m UA
ndA U A
So if we want to measure volume flow rate, we need somethingsensitive to average velocity.
If we want to measure mass flow rate, we need something to average
mass flux
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15.2 Flow Characteristics
Laminar/Turbulent determined by Reynolds number
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Volume Flow Rate Measurement
Brute Force Method. Measure the velocity, do the integral.
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Bernoullis Equation
P1 P2
V2
2 V12
2gc
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Obstruction Meters
P1
P2
V2
2 V1
2
2gc
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15.3.1 Obstruction Meters
for = const
p1
V1
2
2
p2
V2
2
2
Qideal V2A2 A2
1 A2 /A1 2
1/ 22gc P1 P2
V1 A2A1
V2
P1 P2 V2
2
2gc1 A2 /A1
2
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Velocity Approach Factor
E1
1 A2 /A1 2
1/ 2
For round pipes, make b= d/D where d is the smaller diameter whileD
is the larger,
E1
1b4
CQactual
Qideal
K CEC
1b4
discharge coefficient
flow coefficient
Qactual KA22gc P1 P2
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Venturi Meters
0.95 < C< 0.98
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Flow Nozzles
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Bore diameters from 0.375 to 24
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Orifice Flow Meters
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Losses in Orifice Flow Meters
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Relative performance
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Application
h k d l d i l
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Choked Flow and Sonic Nozzles
If the flow inside of one of these devices becomes sonic, the mass
flow rate becomes fixed with changes in the downstream pressure.This can be used to limit the mass flow, and can also be something to
be avoided, because when it occurs, our calibrations we have been
talking about are no longer valid. Choked flow exists if
po
p1
2
k1
k/ k1
We can use this fact to fix the mass
flow at a value equal to
m 1A 2RT1k
k12
k1
2
k1
i l l
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Laminar Flow Elements
The obstruction meters are something you are most likely to see in an
industrial setting, since they are cheap and rugged. If more accuracy isdesired, and you have more money and you arent flowing something
really nasty, a laminar flow element may be more appropriate.
Remember that flow is laminar at small Reynolds number:Re = UD/n.
This tells us that we can make flow laminar if we put it through a
sufficiently smallD.
L i Fl El
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Laminar Flow Elements
We do this because the pressure drop/flow rate relationship for
laminar flow is very nicely behaved:
Q d1
4
128
p1 p2L
Re 2000
The important part is the fact that Q varies linearly with DP. Once again,the manufacturer of this meter will provide the sensitivity.
M i L i Fl El
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Meriam Laminar Flow Elements
R
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Rotameters
Q AwC2gf f w
Afw
1/ 2
Aw 4
D by 2 d2
2% full scale
T bi Fl M
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Turbine Flow Meters
1/2%
V Sh ddi M
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Vortex Shedding Meters
StfD
V
V t Sh ddi M t
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Vortex Shedding Meters
St fDV
V t Sh ddi M t
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Vortex Shedding Meters
Q K1
K1
d3
4St
M Fl M t
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Mass Flow Meters
Thermal Flow Meter 1st law, ideal gas:
E m cpDT
Ch M Fl M t
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Cheaper Mass Flow Meters
Old S h l
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Old School
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St ti P
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Static Pressure
A very fortunate result of boundary layer theory tells is that the
pressure gradient normal to a wall is negligible. This means that if we
measure the pressure at the wall, it is the same as in the bulk fluid. So,
we can put a small hole in the wall of whatever we are looking at and
measure the pressure there.
V l it Pit t St ti P b
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Velocity--Pitot-Static Probe
ps
Us2
2
pT
UT2
2
Us 2pT ps
Us2 DP
2 U
dDP
2
DP2 1
DP
2
Pitot probe errors
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Pitot probe errors
Kiel Probes
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Kiel Probes
Static Pressure Probes
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Static Pressure Probes
Transmission Effects
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Transmission Effects
Many times, the pressure is transmitted to a sensor via some sort of
flexible tube. This tube will effect the response of the system, andwe need to be careful that it does not affect our results.
Thermal Anemometry
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Thermal Anemometry
Particle Image Velocimetry
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Particle Image Velocimetry
PIV
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PIV
PIV data
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PIV data
Flow meter calibration
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Flow meter calibration