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Pressure Measurements


         Material prepared
                 by
Alessandro Talamelli, Antonio Segalini
                  &
        P. Henrik Alfredsson
Literature
•  Springer Handbook of Experimental Fluid
   Mechanics, Cameron Tropea,
   Alexander L. Yarin , John F. Foss (2007),
   ISBN-10: 3540251413

•     Measurement in Fluid Mechanics
     Stavros Tavoularis, Cambridge University Press
     (2009) ISBN-10: 0521138396

•  Fluid Mechanics Measurements, R. Goldstein,
   CRC Press; (1996) ISBN-10: 156032306X

•  Low-Speed Wind Tunnel Testing,
   Jewel B. Barlow , William H. Rae, Alan Pope,
   Wiley-Interscience; (1999) ISBN-10:
   0471557749
Measurement techniques

•  Type of Measurements

  –  Local measurements
  –  Integral measurements

  –  Direct measurements
  –  Non-direct measurements

  –  Field measurements
  –  Surface measurements

  –  Time averaged measurements
  –  Time resolved measurements
Measurement chain
          Sensor



        Transducer



  Acquisition data systems



  Evaluation data systems
Sensor
•  Element which changes its status when
   in contact with the quantity to be
   measured
Sensor characteristics I
 •  Spatial and temporal resolution




Spatial and temporal resolutions are coupled because it is not
generally possible to distinguish if the quantity to be
measured varies with time or if there are pseudo-temporal
variations caused by the passage of spatial disturbances.
Sensor characteristics II
•  Accuracy
•  Intrusivity: Non-intrusive methods are really
  non-intrusive (?)
•  Interference
•  Robustness
•  Calibration
•  Linearity
•  Cost
Transducer
•  Element which transforms the changes
   in the sensor s status in an output
    signal
•  Typically it is an electrical signal
Ideal sensor/transducer
                                             Output Signal

                                                                S(t)
     Physical Quantity   Sensor and Transducer              s


•  Output signal is proportional to the
   magnitude of the physical quantity                                       u
•  The physical quantity is measured at a                   y

   point in space
•  The output signal represents the input
                                                                         u( x, y, z)


   without frequency distortion                     z                       x

•  Low noise on output signal
•  Sensor does not interfere with the                   s

   physical process                                                    ! ! !s(t )

•  Output is not influenced by other
                                                                       ! ! !u(t )

                                                                        t
   variables
Basic Definitions I
In an internal point of a fluid the pressure
can be defined as the mean of the three
normal stress components acting over three
surface elements orthogonal to each other in
the point at rest with respect to the fluid.
For a fluid in motion this value is called static
pressure (definition by Aeronautical
Research Council ).
Basic Definitions II
If the fluid is brought to rest with an
isentropic and adiabatic process, the pressure
rises until a maximum that is called the total
pressure.
The stagnation pressure is the pressure
measured when the velocity is zero.
The dynamic pressure is the difference
between the total and the static pressure.

              pdyn = ptot - ps
Basic definitions III

If the Bernoulli s law is valid we have
                       1   2
            ptot = ps + !V
                       2
which give us
                     1
             pdyn   = ρV 2
                     2
Otherwise: the kinetic pressure is

                     1
             pkin   = ρV 2
                     2
Static pressure
Ideally the static pressure should be measured with a
pressure probe that moves at the same velocity as
the fluid particle. But unpractical!


Instead chose a stationary probe with respect to the
laboratory (or airplane), choose a suitable shape and
position the probe in a place where the pressure is
equal to the static pressure of the undisturbed flow.
Static pressure probe
STATIC PROBES

Presence of holes at a distance of 3D from the
leading edge and 8-10D from the stem.
                                  s




Sensitivity to the inclination of the asymptotic flow
with respect to the probe axis.
                                                    s
Static pressure probe
•  WALL TAPPINGS
•  On a wing or in pipes and ducts the static
   pressure can be measured using holes in the
   surface (give attention to the sensitivity of
   the dimensions and the shape of the holes).




                            ps-patm

                                               s
Static probes
•  The probe must be aligned with the flow (this
   effect can be reduced by using several holes)
•  Since the pressure is measured with holes,
   then the same problems of the wall tappings
   must be considered
  –  Effects of tip shape (geometry depends from flow
     regime)
  –  Effects of probe blockage
  –  Effects of hole position
  –  Effects of the support
Blockage effect




•  Nose acceleration and probe support
   effects may compensate
Wall tappings
•  The flow is very complex in proximity of the
   tapping (only low Re simulations)
  –    Effects of orifice shape
  –    Effects of orifice orientation
  –    Effects of surface orientation
  –    Shape and position of the cavity (minimum depth)
  –    Compressibility
  –    Effects of the tapping orifice condition
  –    Effect of the distance from the measured point
Effect of d+




                         McKeon and Smits MST (2002)

•  More problematic for high Re
Effect of d+




                          McKeon and Smits MST (2002)

•  Less influence when d increases
Total pressure probe
The stagnation pressure is obtained when the
fluid is brought to rest through an isentropic and
adiabatic process.
In subsonic flow the Pitot tube measures the
stagnation pressure
(French hydraulic engineer 1695-1771)
Total pressure probe
•  In supersonic flow there is a stagnation pressure
   loss over the shock wave that is formed in front
   of the tube
•  Flat, hemisherical or elliptic head. In supersonic
   flow typically sharp wedge front.
Total pressure
           p0 m − p                    u '2 v'2 w'2    y
      Cp =          = f (ϑ , Re d , M , 2 , 2 , 2 , α , )
           1                           U U U           d
              ρU 2
           2

•    Incoming flow direction
•    Local Reynolds number (viscosity)
•    Mach number
•    Velocity gradient
•    Wall proximity
•    Turbulence
Total pressure probe

•  Effects of finite dimensions
  –  Pressure measured in a finite region (not a
     single streamline) -> spatial averaging
  –  This effect can be limited with small probes
     (be careful! : robustness, time response)
  –  Blockage (d/L)
•  Directional sensitivity
Total pressure probe –
         direction sensitivity
Less sensitivity to the inclination of the flow in respect
to the longitudinal axis than the static pressure probe.




                                          From Chue
Total pressure probe

•  Effects of viscosity (in high Reynolds
   number measurement Red can be low due to
   the small dimensions of the probe)
•  Viscous effect are negligible for ReD>100
•  For ReD>30
                          10
                C p = 1 + 1.5
                         Re d
Total pressure – velocity gradient
1) Indicated Pitot pressure > total pressure of the
undisturbed flow if a Pitot tube is operated in a region
where the total pressure varies in a direction ortoghonal
to the asymptotic flow (e.g Boundary layer).
Total pressure – velocity gradient
1) Velocity gradient interference


2) With the presence of a flat wall parallel to the probe
axis there could be a reflection effect with the
consequent measured pressure higher than the total
pressure. This effect is negligible for y>2d from the wall.




                        McKeon, Li, Jiang, Morrison and Smits MST (2003)
Total pressure – velocity gradient

•  Error 1) is normally corrected by changing the
   probe position rather than correcting the flow
                Δy
   velocity        = ε , ε = 0.15 ( MacMillan)
              d
             Δy                               d       dU
                = 0.18α (1 − 0.17α 2 ), α =                    ( Zagarola )
             d                              2U ( yc ) dy   c
             Δy
                = 0.15 tanh(4 α ),      ( McKeon)
              d
•  This is based on analytical displacement
   correction for a sphere in a velocity gradient
Total pressure – velocity gradient

•  Wall correction
           ΔU            ⎡     ⎛ y     ⎞⎤
              = 0.015 exp⎢− 3.5⎜ − 0.5 ⎟⎥ ( MacMillan)
           U             ⎣     ⎝ d     ⎠⎦


•  A new correction is proposed based on Preston
   probe pressure data
                      ⎧    0.150 for d + < 8
                 δ w ⎪
                    = ⎨ 0.120 for 8 < d + < 110
                  d ⎪
                      ⎩0.085 for 110 < d + < 1600
How important wall
 correction are ?




       McKeon, Li, Jiang, Morrison and Smits MST (2003)
Velocity measurements with differential
      pressure probe: the Prandtl probe

•  Steady flow, low velocity, viscosity negligible:
   Bernoulli s law holds
                1
     ptot = ps + !V 2
                2
•  High velocity:
                1
     ptot = ps + "V 2 ( + ! p )
                      1
                2
                                  Corrective term f(M)

            2(ptot # pst )
         V=
             "( + ! p )
               1
Measurement errors due to
           turbulence
A physical time-dependent quantity can generally be
splitted in a mean part and in a fluctuating part
             v(t ) = V + v' (t )   p (t ) = P + p ' (t )
From Bernoulli s law:
                                      1
                                           (
         Ptot + p 'tot = Pst + p 'st + ! V 2 + 2Vv'+v'2
                                      2
                                                               )
Taking the time-average:
                              1   2
                                     (
                  Ptot = Pst + ρ V + v'
                              2
                                        2
                                                 )         Error due to
                                                           fluctuating
                                                           velocity
Effect of the anisotropy
Measurement errors due to
         turbulence
Another effect is linked to the radial gradient of
the static pressure due to the fluctuations


This is of the opposite sign than the turbulence one.
Therefore they compensate.
Velocity measurements - compressibility
                effects




Μ     εp                         εp
0     0
0.1   0.0025
0.2   0.010
0.3   0.023
                Note that the error in velocity is
0.5   0.083
                about half of εp !
1.0   0.274
Velocity measurements at a nozzle exit


V1 , A1 , p1                 Vexit , Aexit , pexit

•  Mass conservation equation:

                                 V1 A1 = Vexit Aexit
•  Bernoulli s law applied to a streamline passing on the
   reference section and to the nozzle exit:
                               1   2         1   2
                           p1 + !V1 = pexit + !Vexit
                               2             2
Velocity measurements at a nozzle exit


•  Combining the two relations:

                            2(p
              Vexit =           2
                          & Aexit   #
                        ) $1 ' 2
                          $         !
                                    !
                          %   A1    "

•  If section 1 is characterized by a dimension much
   larger then the exit s one, the corrective term
   can be neglected
Pressure transducers
Absolute pressure transducer
Measures the pressure relative to perfect vacuum pressure.
(Example: barometer, used also for compressible flow)

Gauge pressure transducer
Measures the pressure relative to a given atmospheric pressure
at a given location. (Example a tire pressure gauge).

Vacuum pressure transducer
This sensor is used to measure small pressures less than the
atmospheric pressure.

Differential pressure transducer
This sensor measures the difference between two or more
pressures introduced as inputs to the sensing unit.
                                                                 s
Pressure transducers




           pd =ρ h sin(θ)
                            s
Pressure transducers




Betz manometer




                                  s
Differential Pressure transducers

Capacitance principle




 •  Very accurate
 •  Need to be calibrated (time to time)
                                             s
 •  Expensive for multi point measurements
Pressure transducers




•  Need to be calibrate
                             s
Pressure Scanners




•  Important in pipe/channel turbulence
Multi component velocity measurements

•  Five hole Pitot




•  Pressure distributions on the probe s head is
   function of its geometry and of the flow
   direction
•  By sampling this distribution in five points is
   possible to determine the direction and
   magnitude of the velocity vector
Multi component velocity measurements

               Calibration
Time resolved pressure measurements



•  Microphone: electromechanical transducer. The
   sensing element is a thin membrane that alters
   its shape under the pressure loading effect


•  High capacity to measure the pressure variations
   in the measurement point (the sensor measures
   variations up to at least 5 kHZ)
Time resolved pressure measurements

•  Capacitive type




•  Piezoelectric type




•  strain measurements
Time resolved pressure measurements

Pressure probe for measurements of pressure
fluctuations inside the boundary layer (Tsuji et al
2007)
Time resolved pressure measurements

Frequency response for pressure probe of Tsuji
et al. Frequenct is normalized with Helmholz
resonator frequency.
Time resolved pressure measurements

Measured rms fluctuations of the pressure inside
turbulent boundary layers at different Re. Lines
are from numerical simulations.
Sensor characteristics
•  Resolution √
•  Frequency response X
•  Accuracy √
•  Intrusivity X
•  Interference X
•  Robustness √
•  Calibration (X)
•  Linearity √
•  Cost √

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Lecture pressure 2012

  • 1. Pressure Measurements Material prepared by Alessandro Talamelli, Antonio Segalini & P. Henrik Alfredsson
  • 2. Literature •  Springer Handbook of Experimental Fluid Mechanics, Cameron Tropea, Alexander L. Yarin , John F. Foss (2007), ISBN-10: 3540251413 •  Measurement in Fluid Mechanics Stavros Tavoularis, Cambridge University Press (2009) ISBN-10: 0521138396 •  Fluid Mechanics Measurements, R. Goldstein, CRC Press; (1996) ISBN-10: 156032306X •  Low-Speed Wind Tunnel Testing, Jewel B. Barlow , William H. Rae, Alan Pope, Wiley-Interscience; (1999) ISBN-10: 0471557749
  • 3. Measurement techniques •  Type of Measurements –  Local measurements –  Integral measurements –  Direct measurements –  Non-direct measurements –  Field measurements –  Surface measurements –  Time averaged measurements –  Time resolved measurements
  • 4. Measurement chain Sensor Transducer Acquisition data systems Evaluation data systems
  • 5. Sensor •  Element which changes its status when in contact with the quantity to be measured
  • 6. Sensor characteristics I •  Spatial and temporal resolution Spatial and temporal resolutions are coupled because it is not generally possible to distinguish if the quantity to be measured varies with time or if there are pseudo-temporal variations caused by the passage of spatial disturbances.
  • 7. Sensor characteristics II •  Accuracy •  Intrusivity: Non-intrusive methods are really non-intrusive (?) •  Interference •  Robustness •  Calibration •  Linearity •  Cost
  • 8. Transducer •  Element which transforms the changes in the sensor s status in an output signal •  Typically it is an electrical signal
  • 9. Ideal sensor/transducer Output Signal S(t) Physical Quantity Sensor and Transducer s •  Output signal is proportional to the magnitude of the physical quantity u •  The physical quantity is measured at a y point in space •  The output signal represents the input u( x, y, z) without frequency distortion z x •  Low noise on output signal •  Sensor does not interfere with the s physical process ! ! !s(t ) •  Output is not influenced by other ! ! !u(t ) t variables
  • 10. Basic Definitions I In an internal point of a fluid the pressure can be defined as the mean of the three normal stress components acting over three surface elements orthogonal to each other in the point at rest with respect to the fluid. For a fluid in motion this value is called static pressure (definition by Aeronautical Research Council ).
  • 11. Basic Definitions II If the fluid is brought to rest with an isentropic and adiabatic process, the pressure rises until a maximum that is called the total pressure. The stagnation pressure is the pressure measured when the velocity is zero. The dynamic pressure is the difference between the total and the static pressure. pdyn = ptot - ps
  • 12. Basic definitions III If the Bernoulli s law is valid we have 1 2 ptot = ps + !V 2 which give us 1 pdyn = ρV 2 2 Otherwise: the kinetic pressure is 1 pkin = ρV 2 2
  • 13. Static pressure Ideally the static pressure should be measured with a pressure probe that moves at the same velocity as the fluid particle. But unpractical! Instead chose a stationary probe with respect to the laboratory (or airplane), choose a suitable shape and position the probe in a place where the pressure is equal to the static pressure of the undisturbed flow.
  • 14. Static pressure probe STATIC PROBES Presence of holes at a distance of 3D from the leading edge and 8-10D from the stem. s Sensitivity to the inclination of the asymptotic flow with respect to the probe axis. s
  • 15. Static pressure probe •  WALL TAPPINGS •  On a wing or in pipes and ducts the static pressure can be measured using holes in the surface (give attention to the sensitivity of the dimensions and the shape of the holes). ps-patm s
  • 16. Static probes •  The probe must be aligned with the flow (this effect can be reduced by using several holes) •  Since the pressure is measured with holes, then the same problems of the wall tappings must be considered –  Effects of tip shape (geometry depends from flow regime) –  Effects of probe blockage –  Effects of hole position –  Effects of the support
  • 17. Blockage effect •  Nose acceleration and probe support effects may compensate
  • 18. Wall tappings •  The flow is very complex in proximity of the tapping (only low Re simulations) –  Effects of orifice shape –  Effects of orifice orientation –  Effects of surface orientation –  Shape and position of the cavity (minimum depth) –  Compressibility –  Effects of the tapping orifice condition –  Effect of the distance from the measured point
  • 19. Effect of d+ McKeon and Smits MST (2002) •  More problematic for high Re
  • 20. Effect of d+ McKeon and Smits MST (2002) •  Less influence when d increases
  • 21. Total pressure probe The stagnation pressure is obtained when the fluid is brought to rest through an isentropic and adiabatic process. In subsonic flow the Pitot tube measures the stagnation pressure (French hydraulic engineer 1695-1771)
  • 22. Total pressure probe •  In supersonic flow there is a stagnation pressure loss over the shock wave that is formed in front of the tube •  Flat, hemisherical or elliptic head. In supersonic flow typically sharp wedge front.
  • 23. Total pressure p0 m − p u '2 v'2 w'2 y Cp = = f (ϑ , Re d , M , 2 , 2 , 2 , α , ) 1 U U U d ρU 2 2 •  Incoming flow direction •  Local Reynolds number (viscosity) •  Mach number •  Velocity gradient •  Wall proximity •  Turbulence
  • 24. Total pressure probe •  Effects of finite dimensions –  Pressure measured in a finite region (not a single streamline) -> spatial averaging –  This effect can be limited with small probes (be careful! : robustness, time response) –  Blockage (d/L) •  Directional sensitivity
  • 25. Total pressure probe – direction sensitivity Less sensitivity to the inclination of the flow in respect to the longitudinal axis than the static pressure probe. From Chue
  • 26. Total pressure probe •  Effects of viscosity (in high Reynolds number measurement Red can be low due to the small dimensions of the probe) •  Viscous effect are negligible for ReD>100 •  For ReD>30 10 C p = 1 + 1.5 Re d
  • 27. Total pressure – velocity gradient 1) Indicated Pitot pressure > total pressure of the undisturbed flow if a Pitot tube is operated in a region where the total pressure varies in a direction ortoghonal to the asymptotic flow (e.g Boundary layer).
  • 28. Total pressure – velocity gradient 1) Velocity gradient interference 2) With the presence of a flat wall parallel to the probe axis there could be a reflection effect with the consequent measured pressure higher than the total pressure. This effect is negligible for y>2d from the wall. McKeon, Li, Jiang, Morrison and Smits MST (2003)
  • 29. Total pressure – velocity gradient •  Error 1) is normally corrected by changing the probe position rather than correcting the flow Δy velocity = ε , ε = 0.15 ( MacMillan) d Δy d dU = 0.18α (1 − 0.17α 2 ), α = ( Zagarola ) d 2U ( yc ) dy c Δy = 0.15 tanh(4 α ), ( McKeon) d •  This is based on analytical displacement correction for a sphere in a velocity gradient
  • 30. Total pressure – velocity gradient •  Wall correction ΔU ⎡ ⎛ y ⎞⎤ = 0.015 exp⎢− 3.5⎜ − 0.5 ⎟⎥ ( MacMillan) U ⎣ ⎝ d ⎠⎦ •  A new correction is proposed based on Preston probe pressure data ⎧ 0.150 for d + < 8 δ w ⎪ = ⎨ 0.120 for 8 < d + < 110 d ⎪ ⎩0.085 for 110 < d + < 1600
  • 31. How important wall correction are ? McKeon, Li, Jiang, Morrison and Smits MST (2003)
  • 32. Velocity measurements with differential pressure probe: the Prandtl probe •  Steady flow, low velocity, viscosity negligible: Bernoulli s law holds 1 ptot = ps + !V 2 2 •  High velocity: 1 ptot = ps + "V 2 ( + ! p ) 1 2 Corrective term f(M) 2(ptot # pst ) V= "( + ! p ) 1
  • 33. Measurement errors due to turbulence A physical time-dependent quantity can generally be splitted in a mean part and in a fluctuating part v(t ) = V + v' (t ) p (t ) = P + p ' (t ) From Bernoulli s law: 1 ( Ptot + p 'tot = Pst + p 'st + ! V 2 + 2Vv'+v'2 2 ) Taking the time-average: 1 2 ( Ptot = Pst + ρ V + v' 2 2 ) Error due to fluctuating velocity Effect of the anisotropy
  • 34. Measurement errors due to turbulence Another effect is linked to the radial gradient of the static pressure due to the fluctuations This is of the opposite sign than the turbulence one. Therefore they compensate.
  • 35. Velocity measurements - compressibility effects Μ εp εp 0 0 0.1 0.0025 0.2 0.010 0.3 0.023 Note that the error in velocity is 0.5 0.083 about half of εp ! 1.0 0.274
  • 36. Velocity measurements at a nozzle exit V1 , A1 , p1 Vexit , Aexit , pexit •  Mass conservation equation: V1 A1 = Vexit Aexit •  Bernoulli s law applied to a streamline passing on the reference section and to the nozzle exit: 1 2 1 2 p1 + !V1 = pexit + !Vexit 2 2
  • 37. Velocity measurements at a nozzle exit •  Combining the two relations: 2(p Vexit = 2 & Aexit # ) $1 ' 2 $ ! ! % A1 " •  If section 1 is characterized by a dimension much larger then the exit s one, the corrective term can be neglected
  • 38. Pressure transducers Absolute pressure transducer Measures the pressure relative to perfect vacuum pressure. (Example: barometer, used also for compressible flow) Gauge pressure transducer Measures the pressure relative to a given atmospheric pressure at a given location. (Example a tire pressure gauge). Vacuum pressure transducer This sensor is used to measure small pressures less than the atmospheric pressure. Differential pressure transducer This sensor measures the difference between two or more pressures introduced as inputs to the sensing unit. s
  • 39. Pressure transducers pd =ρ h sin(θ) s
  • 41. Differential Pressure transducers Capacitance principle •  Very accurate •  Need to be calibrated (time to time) s •  Expensive for multi point measurements
  • 42. Pressure transducers •  Need to be calibrate s
  • 43. Pressure Scanners •  Important in pipe/channel turbulence
  • 44. Multi component velocity measurements •  Five hole Pitot •  Pressure distributions on the probe s head is function of its geometry and of the flow direction •  By sampling this distribution in five points is possible to determine the direction and magnitude of the velocity vector
  • 45. Multi component velocity measurements Calibration
  • 46. Time resolved pressure measurements •  Microphone: electromechanical transducer. The sensing element is a thin membrane that alters its shape under the pressure loading effect •  High capacity to measure the pressure variations in the measurement point (the sensor measures variations up to at least 5 kHZ)
  • 47. Time resolved pressure measurements •  Capacitive type •  Piezoelectric type •  strain measurements
  • 48. Time resolved pressure measurements Pressure probe for measurements of pressure fluctuations inside the boundary layer (Tsuji et al 2007)
  • 49. Time resolved pressure measurements Frequency response for pressure probe of Tsuji et al. Frequenct is normalized with Helmholz resonator frequency.
  • 50. Time resolved pressure measurements Measured rms fluctuations of the pressure inside turbulent boundary layers at different Re. Lines are from numerical simulations.
  • 51. Sensor characteristics •  Resolution √ •  Frequency response X •  Accuracy √ •  Intrusivity X •  Interference X •  Robustness √ •  Calibration (X) •  Linearity √ •  Cost √