turbulent flow viscosity

Upload: dasaka-brahmendra

Post on 07-Jul-2018

226 views

Category:

Documents


0 download

TRANSCRIPT

  • 8/18/2019 Turbulent Flow Viscosity

    1/12

    15th Int Symp on Applications of Laser Techniques to Fluid MechanicsLisbon, Portugal, 05-08 July, 2010

    - 1 -

    Wall shear stress distribution in a turbulent channel flow

    Omid Amili1, Julio Soria

    2

    1: Laboratory for Turbulence Research in Aerospace and Combustion, Department of Mechanical and AerospaceEngineering, Monash University, VIC 3800, AUSTRALIA

    [email protected]

    2: Laboratory for Turbulence Research in Aerospace and Combustion, Department of Mechanical and AerospaceEngineering, Monash University, VIC 3800, AUSTRALIA

     [email protected]

    Abstract  A film-based wall shear stress sensor has been used to measure dynamic wall shear stress

    distribution in a turbulent channel flow. The sensor which used to directly measure the wall shear stress

    consists of mounting a thin flexible film on the solid surface. The sensor is made of a homogeneous,

    isotropic, and incompressible material. The geometry and mechanical properties of the film are measured,

    and particles with the nominal size of 11 µm in diameter are embedded on the film’s surface to act as

    markers. An optical technique is used to measure the in-plane film deformation caused by the flow. The filmhas typically deflection of less than 2% of the material thickness under maximum loading. The sensor

    sensitivity can be adjusted by changing the thickness of the layer or the shear modulus of the film’s material.

    For this study, a film with the shear modulus of 80 Pa and 2 mm in thickness was used. The sensor is

    statically calibrated by applying a constant shear stress to the top surface of the film showing an excellent

    linear stress-strain relationship. The dynamic response of the sensor has been measured using a dynamic

    calibration apparatus and procedure developed specifically for this purpose. The sensor transfer function

    shows a low-pass behavior. Measurements have been performed in a fully developed turbulent channel flow

    at the Reynolds number of 130,000 based on the bulk velocity and channel full height. The results, which are

    compared with the available results in the literature, show the capacity of the technique to dynamically

    measure wall shear stress over an extended area of the surface. Distribution measurement of the fluctuating

    wall shear stress reveals the imprint of small-scale hairpins or counter-rotating streamwise vortex pairs

    existing in the near-wall region.

    1. Introduction

    In turbulence research, to understand the dynamics of the near wall momentum transfer, high spatial

    resolution measurements of dynamic wall shear stress distribution are needed. The measurements

    should be performed in a non-intrusive way that does not affect the flow field itself. In addition, the

    measurement field of view should be extensive enough to detect the largest turbulent structures. It is

    also important that measurements can detect a wide range of scales of the shear stress fluctuations.

    Furthermore, it is desired that the shear stress measuring techniques possess an adequate dynamic

     bandwidth to detect all frequency contents usually in the range of a few kHz depending on the fluid

    and flow properties. As a result, determination of wall shear stress using a sensor which fulfills

    these characteristics is a critical and challenging task.

    Due to the high demand on the ability to measure the magnitude, direction, and distribution of wall

    shear stress, a large number of studies have been performed. The shear stress measurement

    techniques are usually divided into direct and indirect methods (Naughton and Sheplak, 2002;

    Fernholz et al, 1996). The large group of indirect shear stress measuring techniques includes the

    obstacle-in-flow methods, velocity profile measurement, and application of heat or mass transfer

    analogies. On the other hand, the small group of direct skin friction measuring techniques currently

    available is mostly based on a floating element which responds to the force applied by the fluid on

    the element. Direct measuring methods are preferable as they directly measure the applied force bythe fluid with no assumption of the flow field. However, they are accompanied with different errors

  • 8/18/2019 Turbulent Flow Viscosity

    2/12

    15th Int Symp on Applications of Laser Techniques to Fluid MechanicsLisbon, Portugal, 05-08 July, 2010

    - 2 -

    and limitations which are well descried in Winter (1977) and Haritonidis (1989). Micro-electro-

    mechanical systems (MEMS) technology has removed many of the limitations existing in

    conventional mechanical fabrications (Schmidt et al, 1988; Lofdahl and Gad-el Hak, 1999; Sheplak

    et al, 2004). However, the nature of the sensors is not suitable for unclean environments and they

    also need further development to become standard and reliable measuring tools (Naughton and

    Sheplak, 2002).Among different developed techniques, the thin-oil-film and liquid-crystal-coating techniques

    which are quasi-direct means of shear stress measurement are able to determine stress distribution.

    Thin-oil-film techniques which have been widely used for the last two decades are based on the

     behavior of the oil film under shear loading. The oil thinning rate responds to changes of shear

    stress with a bandwidth in the 10 kHz range (Naughton and Brown, 1999). The major uncertainty

    arising from the difficulty of precisely measuring the oil viscosity was reported within 4% by

    Fernholz et al (1996) and was evaluated less than 2.4% in the range of investigated shear stress by

    Zanoun et al (2003). In liquid-crystal technique, the temporal resolution of measuring the two-

    dimensional wall shear stress distribution is in the range of a few kHz (Fujisawa et al, 2003).

    Although it was introduced more than three decades ago, different problems including measurement

    uncertainty of 5% in the shear stress magnitude have made the technique unsuitable for manyturbulent flow applications (Naughton and Sheplak, 2002).

    A novel type of sensor which has the potential to measure the mean and fluctuating wall shear stress

    distribution using a flexible material has been proposed in recent years. Micro-pillar shear stress

    sensor (MPS3), able to measure dynamic wall shear stress in turbulent flows, is based on flexible

    micro-pillars immersing in the viscous sublayer (Grosse and Schroder, 2008a,b). Depending on the

     pillar dimensions and mechanical properties, length scales better than 50 µm and time scales in the

    range of a few kHz can be resolved. The sensor length to diameter ratio is between 15 and 25 and

    the Young’s modulus is in the order of a few MPa. The optical detection and array of micro pillars

    allow the high spatial resolution determination of the two-dimensional shear stress (Grosse, 2008).

    The surface shear sensitive film (S3F) is another sensor which takes advantage of using a linear

    elastic material. This technique was first introduced by Tarasov and Orlov in the early 1990s as a

    direct method for measuring wall shear stress (cited in Tarasov et al (1997)). A thin elastomer layer

    is mounted on the solid surface subjected to a flow field and its resulting viscous shear stress is

    determined using Hooke’s law from the film deformation. The experimental setup similar to the

     pressure sensitive paint (PSP) technique includes a surface or volume-distributed transducer, a light

    source, and an image and data acquisition system (Fonov et al, 2006a,b, 2007). However, unlike

    PSP which can only be used in air, this technique can be used in most fluids since it does not

    depend on oxygen quenching. McQuilling et al (2008) and Crafton et al (2008) claimed sensor

    fabrication with frequency response up to 1 kHz with the shear modulus ranging from 30 Pa to a

    few hundred kPa. In these studies, the film response estimation is based on finite element modeling

    of the film under unit normal and tangential applied loads. McQuilling et al (2008) verified thetechnique using an oil film shear stress measurement in the range of 0.25 to 1.5 Pa and observed a

    difference of 0.25-0.33 Pa. Crafton et al (2008) estimated the accuracy in the tangential

    displacement detection of 0.05 px (equivalent to 0.3 µm) corresponding to an error of 25 Pa in the

    shear stress measurements in the range of 50 to 500 Pa.

    The present study is aimed at measuring dynamic wall shear stress in a turbulent channel flow using

    an in-house developed film-based shear stress sensor at the Laboratory for Turbulence Research in

    Aerospace and Combustion (LTRAC) at Monash University. The feasibility of the technique

    concept to detect mean wall shear stress has been demonstrated by developing and applying the

    sensor to the same flow facility at Reynolds numbers in the range of 90,000-130,000 based on the

     bulk velocity and channel full height (Amili et al, 2009; Amili and Soria, 2009; Amili and Soria,

    2010). A brief description of the sensor, film fabrication, static and dynamic calibration, and flowfacility is given here. More detailed information can be found in the cited works. The sensor

  • 8/18/2019 Turbulent Flow Viscosity

    3/12

    15th Int Symp on Applications of Laser Techniques to Fluid MechanicsLisbon, Portugal, 05-08 July, 2010

    - 3 -

    capability of dynamically detecting wall shear stress has been assessed by measuring instantaneous

    wall shear stress distribution.

    2. Sensor description

    The film-based shear stress sensor technique is based on mounting a thin layer film made of anelastic material on the solid surface of the model or the test section of the flow facility. The elastic

    layer is created by forming the material at room temperature into a flat rectangular cavity with a

    smooth surface made of glass as fabricated in the study by Amili et al (2009) and Amili and Soria

    (2010). The cavity which is machined into a flat plate was designed to fit into the floor of the wind

    tunnel test section. Depending on the experimental condition, the thickness of the film can be

    adjusted between 0.5 and 3 mm by varying the cavity depth. The geometry and mechanical

     properties of the flexible material were accurately measured. Immediately after the film formation,

    11 µm diameter Potters spherical particles acting as markers are embedded on the film’s top surface

    flush with that surface to minimize the roughness. An optical technique is used to measure the film

    deformation caused by the flow field.

    The film is formed from a material which satisfies the linear elastic solid  characteristics within the

    desired range of operation: the deformations are very small; the relationship between applied loads

    and deformations is linear; upon removal of applied loading, deformations are completely removed;

    the loading rate has no effect on deformations. Owing to the fact that the film layer is made of a

    liquid-based elastic material, it is deformed when loading under incompressibility condition and

    returns to its initial shape after the load is removed. In addition, since the film used for the sensor is

    homogeneous and isotropic, the shear modulus is independent of the location and direction.

    The film deformation is measured using the images of the film while loaded with respect to its

    initial unloaded condition. Then, the shear stress distribution over the film is determined by

    implementing the shear stress-strain relationship which is based on linear continuum mechanics

    (Lai et al, 1993). More information about the governing equations can be found in Amili et al(2009). The film deformation is a function of the applied load, film’s shear modulus, and thickness.

    The sensor geometry and mechanical properties are carefully selected so that the deformation does

    not exceed more than 2% of the film’s thickness under maximum predicted flow loading. In

    addition, the sensor sensitivity can be adjusted by changing these parameters based on the estimated

    shear stress range to be measured. An important advantage of this film-based technique is that

    depending on the employed material, it is applicable to air, water, or any environment where the

    film is not chemically or physically modified by the working fluid.

    In this study we are only concerned with measuring the tangential shear stress and not the surface

     pressure, hence only the in-plane strain deformation of the film is required. The 2D in-plane film

    deformation is measured by means of a 2C-2D cross correlation PIV algorithm (Soria, 1998).

    3. Sensor calibration

    3.1. Static Calibration

    The static calibration of the sensor involves applying a constant shear load on the film’s surface and

    measuring the film deformation under different loading conditions. Detailed information about the

    static calibration stage and the procedure can be found in Amili et al (2010). All the associated

    errors in the calibration step including specifying the loading angle, mass of the load, load contact

    area, and the cross-correlation resolvable displacement have been considered and the overall

    uncertainty of measuring shear modulus based on the 95% level of confidence is estimated to be

     better than 2% of the measured modulus for G

  • 8/18/2019 Turbulent Flow Viscosity

    4/12

    15th Int Symp on Applications of Laser Techniques to Fluid MechanicsLisbon, Portugal, 05-08 July, 2010

    - 4 -

    Figure 1a shows excellent linear behavior with a negligible hysteresis effect for the films developed

    at our laboratory. The non-zero intercept, which pre-loading, hysteresis or any other bias error in the

    measurement system may contribute to, falls within the overall measurement uncertainty. The shear

    modulus is determined from the linear least squares fit to the measured shear stress-strain

    relationship. The Measurements of the shear modulus in three arbitrary directions yields similar

    values within the measurement uncertainty confirming the isotropic assumption. In a similar way, performance of the static calibration at different arbitrary locations of the film proves that the

    homogeneous assumption is true. To date, sensors with the shear modulus between 50 Pa and 3000

    Pa have been developed which possess similar behavior to the sensor shown in Figure 1a.

    Owing to the fact that the sensor is planned to be applied to turbulent shear flows, it is important to

    conduct the calibration in the range of expected wall shear stress values. As a result, calibration is

    carried out in the range of expected mean wall shear stress considering the fluctuations. From the

     probability density function of the wall shear stress or near wall velocity fluctuations in turbulent

    flows reported in the literature (such as Colella and Keith (2003); Monty et al (2007)), fluctuations

    reaching up to four times the mean value can be expected. However, a static calibration curve as

    shown in Figure 1a with a larger range of the applied loading shows in fact that the material

     behaves linearly over a larger range of deformations. Although the calibration is staticallyconducted, a constant shear modulus can be inferred at low loading rates.

    3.2. Dynamic calibration

    The effect of the loading rate on the sensor behavior was investigated via transfer functions

    obtained using a dynamic calibration apparatus and procedure developed for this specific purpose.

    The setup consists of an electro-magnetic vibration exciter (B&K type 4809) capable of producing

    vibrations in the range of 10 Hz to 20 kHz driven by a B&K power amplifier. A HP 33120A

    function generator is used as a high fidelity signal input source and loading is applied via a known

    mass placed on the top surface of the film. A force transducer, and an accelerometer both from

    B&K with the sensitivity of 110 mV/N and 10 mV/ms-2  respectively are used to measure the

    applied force and corresponding acceleration of the mass. These signals are amplified and then

    recorded by means of a computer using an A/D converter. In case of forcing with white noise, a

    low-pass filter (at 2 kHz) is used to create the desired frequency bandwidth. A sample length of

    600,000 for the signals is recorded at 16 kHz rate to ensure a high enough temporal resolution.

    Finding the transfer function to indicate the relation between the input force and the output film

    displacement consists of decomposing the film response into its frequency contents and determining

    the oscillation amplitudes using Fourier analysis. As a result, the amplitude of the film oscillation,

    normalized by a reference amplitude, is determined in terms of frequency. It is worth noting that the

    effective mass applied to the film has been accurately measured via a no-film experiment first.

    The dynamic calibration was conducted for different sensors developed in our laboratory made of

    different materials and different thicknesses. Figure 1b shows the transfer function for the sensorused for this experiment. The transfer function shows low-pass filter behavior with the cut-off

    frequency of 120 Hz. The bandwidth calculation is based on the frequency where the sensor gain

    falls to -3 dB. In the dynamic calibration, the point should be highlighted that all measurements

    have been performed in air and for sensor application in different flow facilities, there is a need for

    calibration in the same working fluid. It is expected that sensors show more damped behavior in

    water because of the damping nature of the fluid.

    For an accurate measurement of the instantaneous wall shear stress, it is important that the sensor

    does not show a gain greater than 1 (i.e. a resonant frequency) in the expected range of frequencies

    that may exist in the wall shear stress signal. Therefore, selection of a suitable sensor with a proper

    shear modulus and thickness is made based on the working fluid and flow properties. The effect of

    geometry and shear modulus of the film on the frequency response of the sensor has beenconsidered. To date, developed sensors in our lab have low-pass filter behavior with the cut-off

  • 8/18/2019 Turbulent Flow Viscosity

    5/12

    15th Int Symp on Applications of Laser Techniques to Fluid MechanicsLisbon, Portugal, 05-08 July, 2010

    - 5 -

    frequency up to 240 Hz. The measurements by Grosse (2008) in a turbulent duct and pipe flow

    show that the highest frequencies of the wall shear stress fluctuations in the streamwise direction

    are less than 500 Hz for comparable Reynolds numbers to this study. This indicates that the sensors

    developed until now in our laboratory are not able to dynamically detect all significant frequencies

    contained in the instantaneous wall shear stress signal. While a sensor with low-pass filter behavior

    has been developed and implemented, further development of a sensor with an increased bandwidthis in progress. It is worth mentioning that to avoid any possible errors caused by changes of the

    film’s mechanical properties or thickness, calibration tests were performed before and after the wall

    shear stress measurement.

    Figure 1. The shear stress-strain curve in a static calibration for the film-based shear stress sensor with the thickness of2 mm. The measurement accuracy is estimated to be better than 0.035 Pa for the applied shear stress and 1.7×10

    −4 Rad

    for the shear strain, (a). The dynamic transfer function for the sensor with the cut-off frequency of 120 Hz, (b).

    4. Experimental setup

    4.1. Flow facility

    Wall shear stress measurements were performed in the open-circuit wind tunnel facility located inthe Laboratory for Turbulence Research in Aerospace and Combustion (LTRAC) at Monash

    University. The flow in the facility is generated by a three-phase 5.5 KW electrical motor coupled

    with an in-line centrifugal blower. The flow rate is accurately controlled by adjusting the motor

    rotational speed by means of a motor controller. The working section is 4.6 m long, 1 m wide, with

    the aspect ratio of 9.75:1. The channel has a large enough aspect ratio which ensures that secondary

    flows in the channel corners do not affect the mean streamwise velocity profile and the turbulent

    fluctuations. The sensor is flush mounted on the lower wall of the test section at a position

    approximately 41 channel height downstream of the test section entrance. The film was formed into

    a cavity with dimensions of 100×70 mm and depth of 1 mm using a perspex plate with dimensions

    of 320×320 mm. The plate was mounted flush with the tunnel wall to prevent any disturbance to the

    local flow field. The experiment was conducted at the Reynolds number of 130,000 based on the bulk flow velocity and the channel full height. At this Reynolds number, based on the PIV

    measurements along the streamwise-wall normal plane, the bulk velocity is 18.55 m/s. The

    turbulence intensity at the centerline of the channel is approximately 1.7%.

    4.2. Optical setup

    Deformation of the film was imaged at 1 KHz using an 8-bit Motion Pro X3 high speed camera at

    full CCD size of 1280×1024 px in combination with a 200 mm Nikkon Micro-Nikkor lens. The F-

    stop of 4 was selected to reduce the depth of field and an array of LEDs was used for particle

    illumination. It is worth noting that to remove any possible rigid-body motion of the sensor caused

     by vibrations of the wind tunnel, a reference pattern attached to the bottom surface of the sensor

     plate was simultaneously recorded. In order to image the reference pattern with the same recordingsystem, a combination of mirrors and prisms were used to split the field of view. As a result, a

    (a) (b)

  • 8/18/2019 Turbulent Flow Viscosity

    6/12

    15th Int Symp on Applications of Laser Techniques to Fluid MechanicsLisbon, Portugal, 05-08 July, 2010

    - 6 -

    narrow strip of the CCD with the approximate size of 256×1024 px was dedicated for this purpose

    and the rest was used for the shear stress measurement. Those movements were subtracted from the

    displacement of the tracer particles on the film’s surface to measure the film’s deflection under flow

    loading. Firstly, particle positions at no-flow condition were recorded as a reference, and then 3270

    images at flow-on state were taken. The sensor used for the experiment has the shear modulus of 80

    Pa and thickness of 2 mm. The schematic of the sensor and imaging system is illustrated in Figure2. The measurements have been performed at T=20°.

    Figure 2. The schematic of the experimental setup for the shear stress measurement.

    5. Wall shear stress measurements

    The multi-grid cross-correlation digital particle image velocimetry (MCCDPIV) algorithm

    developed by Soria (1996, 1998) was used to measure the instantaneous wall shear stressdistribution. Multi-passing with the final interrogation window size of 32×32 px with the step size

    of 16 px at a high sub-pixel accuracy using 2D Gaussian peak-fitting function enables

    measurements with a high dynamic range. This leads to a vector spacing of 185 µm corresponding

    to 10.2 wall units using the imaging resolution of 11.66 µm/px. The field of view is 11.4×11.4 mm

    which is equal to 630×630 wall units.

    5.1. Mean wall shear stress

    The mean film deformation, wall shear stress, friction velocity, and skin friction coefficient have

     been measured at six Reynolds numbers, ReH=90,000-130,000 (Amili et al, 2010). The mean wall

    shear stress calculation is based on the time-average and also the spatial-average of the stress over

    the film located in the entire field of view. The mean stress measurements are in good agreementwith indirect measurements by means of a logarithmic fit to the mean streamwise velocity profile

    obtained from PIV experiments and application of the Clauser method (Amili et al, 2010). The

    measured skin friction compares favorably with the measurements by Zanoun et al (2009),

    Christensen (2001), Monty (2005) and also the logarithmic skin friction relation by Zanoun et al

    (2007).

    In this study, the mean film deflection is approximately 1.5 pixel corresponding to ~1% of the filmthickness. The mean wall shear stress and friction velocity are estimated to be 0.827 Pa and 823

    mm/s respectively. The accuracy of the shear stress measurements is determined by the sub-pixel

    accuracy of the cross-correlation algorithm and the accuracy of the shear modulus determination

    which has been assessed in section 3. The uncertainty of measuring wall shear stress based on the

    95% level of confidence is estimated to be better than 2.5% of the measured stress for τ

  • 8/18/2019 Turbulent Flow Viscosity

    7/12

    15th Int Symp on Applications of Laser Techniques to Fluid MechanicsLisbon, Portugal, 05-08 July, 2010

    - 7 -

    simultaneous measurements of the rigid-body motion of the sensor. The relative movement of the

    sensor with respect to the camera can cause a DC error. As a result, it is independent of the applied

    loading during the experiments and consequently has a greater effect on smaller displacements.

    Figure 3. Example results of the instantaneous fluctuating wall shear stress distribution using a film-based shear stresssensor. The contours indicate the strength of the streamwise fluctuating wall shear stress, τx’/τx,rms in (a) and (c), and

    spanwise fluctuating wall shear stress, τz’/τz,rms in (b) and (d). The field of view is normalized using the friction velocity. 

    5.2. Two-dimensional wall shear stress distribution

    Two example fields of the instantaneous wall shear stress fluctuation distribution are shown in

    Figure 3. The vector field represents the instantaneous wall shear stress fluctuations. The contoursindicate the normalized streamwise fluctuating wall shear stress, τx’/τx,rms  (left) and spanwise

    fluctuating wall shear stress, τz’/τz,rms  (right). The sensor detects the existence of low- and high-

    shear regions aligned in the streamwise direction. By measuring the local wall shear stress

    distribution, the imprint of small-scale hairpins or counter-rotating streamwise vortex pairs existing

    in near-wall region can be captured. These coherent structures reported in the inner layer (Adrian

    (2007); Herpin et at (2008); Jimenez et al (2004)) contribute to the evolution of the fluctuating

    shear stress on the surface. The instantaneous wall shear stress fluctuation distribution is helpful to

    reveal the width of the coherent motions and their spacing.

    5.3. Two-point correlations

    In addition to the qualitative presentation of the fluctuating wall shear stress distribution shown in

    section 5.2, two-point correlations of the fluctuations shows some of the structures’ characteristics.

    (a) (b)

    (c) (d)

  • 8/18/2019 Turbulent Flow Viscosity

    8/12

    15th Int Symp on Applications of Laser Techniques to Fluid MechanicsLisbon, Portugal, 05-08 July, 2010

    - 8 -

    The coherent motions dominate the two-point correlations of the streamwise and spanwise wall

    shear stress fluctuations. Figure 4 shows the two-point correlation of the streamwise wall shear

    stress fluctuations, R τx’τx’ at the wall. Elongated positive correlation region in the streamwise

    direction is accompanied by negative correlation behavior at spanwise sides.

    Figure 4. Contour map of the two-point correlation of the streamwise wall shear stress fluctuations, R τx’ τx’(∆x+

    ,∆z+

    ).

    The two-point correlations of the streamwise wall shear stress fluctuations at ∆z+=0 and at ∆x

    +=0

    are shown in Figure 5a and 5b respectively. While a smooth decay in the correlation is observed in

    the streamwise direction, a strong change in correlation’s sign in the spanwise direction is indicated.

    This supports the findings in pipes, channels, and boundary layers (Hutchins and Marusic, (2007);

    Monty et al (2007); Jeon et al (1999)). In Figure 5b, the spanwise extent of the positive correlation

     provides the average width of the coherent structures in the near wall region. This characteristic

    width of eddies is a function of the Reynolds number and distance from the wall. At the wall, this

    scale is in the order of 100z+. It is reported that it increases as wall distance increases

    (Chernyshenko and Baig (2005); Monty et al (2007)). Furthermore, at a fixed distance from the

    wall, the width scale increases with increasing in Reynolds number (Monty et al, 2007). Based onthe using a correlation threshold of 0.05, the width scale of 244 ℓ

    + is estimated (Reτ=2730).

    Figure 5.  The two-point correlations of the streamwise wall shear stress fluctuations in the streamwise direction,R τx’τx’(∆z

    +=0), (a) and in the spanwise direction, R τx’τx’(∆x+=0), (b). The two-point correlations of the spanwise wall

    shear stress fluctuations in the streamwise direction, R τz’τz’(∆z+=0), (c) and in the spanwise direction, R τz’τz’(∆x

    +=0), (d).

    (c) (d)

    (a) (b)

  • 8/18/2019 Turbulent Flow Viscosity

    9/12

    15th Int Symp on Applications of Laser Techniques to Fluid MechanicsLisbon, Portugal, 05-08 July, 2010

    - 9 -

    In addition, the two-point correlations of the spanwise wall shear stress fluctuations in the

    streamwise and spanwise directions are shown in Figure 4c and 4d respectively. In Figure 5c, a

    stronger decay in the correlation coefficient of R τz’τz’(∆x+) than R τx’τx’(∆x

    +) is observed. The

    spanwise two-point correlations of the streamwise and spanwise wall shear stress fluctuations with

    outer scaling are shown in Figure 6a and 6b for comparison with other wall shear stress estimationsfound in the literature. In spite of the fact that the qualitative behavior of the correlations is similar,

    good collapse can be seen only for ∆z/H>0.05.

    Figure 6. Spanwise two-point correlations of the streamwise wall shear stress fluctuations R τx’τx’(∆x=0), (a) and thespanwise wall shear stress fluctuations, R τz’τz’(∆x=0), (b). The length scale is normalized using the channel full height,H.

    5.4. Probability density functions

    The PDFs of the normalized streamwise and spanwise wall shear stress fluctuations are presented in

    Figure 7a and 7b respectively. The probability density functions are scaled in a way that the integral

    of the PDF by τx’/τx,rms (or τz’/τz,rms) over the range of the fluctuations be 1. The skewness and the

    flatness of the streamwise shear stress fluctuations are calculated as S ƒ =0.21 and F ƒ =3.42respectively. While the flatness is in good agreement with the findings of Colella and Keith (2003),

    and Sheng et al (2008), the fluctuations are less skewed. In the cited works, a longer positive tail for

    the streamwise PDFs, indicating more frequent positive fluctuations, is reported. However,

    measurements by Herpin et at (2008) shows that the streamwise velocity fluctuations near the wall

    (y+

  • 8/18/2019 Turbulent Flow Viscosity

    10/12

    15th Int Symp on Applications of Laser Techniques to Fluid MechanicsLisbon, Portugal, 05-08 July, 2010

    - 10 -

    6. Conclusions

    Instantaneous wall shear stress distribution in a fully developed turbulent channel flow using a film-

     based sensor has been measured. The wall shear stress sensor with the working principle based on

    the deformation of a thin elastic film has been developed and investigated. The advantage of this

    non-intrusive technique is the ability to measure dynamic shear stress distribution based on theevaluated dynamic response measured and demonstrated here. The technique is applicable to air or

    water and its sensitivity can be tuned for different flow conditions by using an available wide range

    of thickness and shear modulus. The technique allows high-spatial resolution measurements of wall

    shear stress with an uncertainty better than 2.5% of the measured stress for

  • 8/18/2019 Turbulent Flow Viscosity

    11/12

    15th Int Symp on Applications of Laser Techniques to Fluid MechanicsLisbon, Portugal, 05-08 July, 2010

    - 11 -

    Fonov SD, Jones EG, Crafton JW, Goss LP, Fonov VS (2007) Measurements of non-steady

     pressure and skin friction fields on wall mounted cube using surface stress sensitive film.

    Collection of Technical Papers - 45th AIAA Aerospace Sciences Meeting 21:15,101–15,110

    Fujisawa N, Aoyama A, Kosaka S (2003) Measurement of shear-stress distribution over a surface

     by liquid-crystal coating. Measurement Science and Technology 14(9):1655–1661

    Grosse S (2008) PhD Thesis, Development of the Micro-Pillar Shear-Stress Sensor MPS3 forturbulent flows. RWTH Aachen University, Germany

    Grosse S, Schroder W (2008a) Dynamic wall-shear stress measurements in turbulent pipe flow

    using the micro-pillar sensor mps3. International Journal of Heat and Fluid Flow 29(3):830–840

    Grosse S, Schroder W (2008b) Mean wall-shear stress measurements using the micro-pillar shear-

    stress sensor mps3. Measurement Science and Technology 19(1)

    Grosse S, Schroder W (2009) Wall-shear stress patterns of coherent structures in turbulent duct

    flow. Journal of Fluid Mechanics 633:147–158

    Haritonidis JH (1989) The measurement of wall shear stress. Advances in Fluid Mechanics

    Measurements pp 229–261

    Herpin S, Wong CY, Stanislas M, Soria J (2008) Stereoscopic piv measurements of a turbulent

     boundary layer with a large spatial dynamic range. Experiments in Fluids 45(4):745–763Hutchins N, Marusic I (2007) Evidence of very long meandering features in the logarithmic region

    of turbulent boundary layers. Journal of Fluid Mechanics 579:1–28

    Jeon S, Choi H, Yoo JY, Moin P (1999) Space-time characteristics of the wall shear-stress

    fluctuations in a low-reynolds-number channel flow. Physics of Fluids 11(10):3084–3094

    Jimenez J, Del Alamo JC, Flores O (2004) The large-scale dynamics of near-wall turbulence.

    Journal of Fluid Mechanics (505):179–199

    Lai WM, Rubin D, Krempl E (1993) Introduction to continuum mechanics, 3rd edn. Butterworth-

    Heinemann

    Lofdahl L, Gad-el Hak M (1999) Mems applications in turbulence and flow control. Progress in

    Aerospace Sciences 35(2):101–203

    McQuilling M, Wolff M, Fonov S, Crafton J, Sondergaard R (2008) An experimental investigation

    of a low-pressure turbine blade suction surface using a shear and stress sensitive film.

    Experiments in Fluids 44(1):73–88

    Monty JP (2005) PhD Thesis, Developments in smooth wall turbulent duct flows. University of

    Melbourne, Australia

    Monty JP, Stewart JA, Williams RC, Chong MS (2007) Large-scale features in turbulent pipe and

    channel flows. Journal of Fluid Mechanics 589:147–156

     Naughton JW, Brown JL (1999) Surface imaging skin friction instrument and method 873352(US

     patent 59633107)

     Naughton JW, Sheplak M (2002) Modern developments in shear-stress measurement. Progress in

    Aerospace Sciences 38(6-7):515–570Schmidt MA, Howe RT, Senturia SD, Haritonidis JH (1988) Design and calibration of a

    microfabricated floating-element shear-stress sensor. IEEE Transactions on Electron Devices

    35(6):750–757

    Sheng J, Malkiel E, & Katz J (2008) Using digital holographic microscopy for simultaneous

    measurements of 3D near wall velocity and wall shear stress in a turbulent boundary layer.

    Experiments in Fluids 45:1023–1035

    Sheplak M, Cattafesta L, Nishida T, McGinley CB (2004) Mems shear stress sensors: Promise and

     progress. AIAA 2004-2606, 24th AIAA Aerodynamic Measurement Technology and Ground

    Testing Conf

    Soria J (1996) An investigation of the near wake of a circular cylinder using a video-based digital

    cross-correlation particle image velocimetry technique. Experimental Thermal and Fluid Science12(2):221–233

  • 8/18/2019 Turbulent Flow Viscosity

    12/12

    15th Int Symp on Applications of Laser Techniques to Fluid MechanicsLisbon, Portugal, 05-08 July, 2010

    - 12 -

    Soria J (1998) Multigrid approach to cross-correlation digital piv and hpiv analysis. Proceedings of

    the 1998 Thirteenth Australasian Fluid Mechanics Conference, Melbourne, Australia, 13-18

    December 1998 pp 381–384

    Tarasov V, Fonov S, Morozov A (1997) New gauges for direct skin friction measurements. Proc of

    17th International Congress on Instrumentation in Aerospace Simulation Facilities (ICIASF)

    Winter KG (1977) Outline of the techniques available for the measurement of skin friction inturbulent boundary layers. Progress in Aerospace Sciences 18(1):1–57

    Zanoun ES, Durst F, Nagib H (2003) Evaluating the law of the wall in two-dimensional fully

    developed turbulent channel flows. Physics of Fluids 15(10):3079–3089

    Zanoun ES, Durst F, Bayoumy O, Al-Salaymeh A (2007) Wall skin friction and mean velocity

     profiles of fully developed turbulent pipe flows. Experimental Thermal and Fluid Science

    32(1):249–261

    Zanoun ES, Nagib HM, Durst F (2009) Refined cf relation for turbulent channels and consequences

    for high re experiments. Fluid DynRes 41:1–12