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

    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=

    ==

    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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