18th International Symposium on the Application of Laser and Imaging Techniques to Fluid Mechanics LISBON PORTUGAL JULY 4 7, 2016.

Similar documents
PIV Measurements of turbulence statistics and near-wall structure of fully developed pipe flow at high Reynolds number

SIMULTANEOUS VELOCITY AND CONCENTRATION MEASUREMENTS OF A TURBULENT JET MIXING FLOW

Simultaneous Velocity and Concentration Measurements of a Turbulent Jet Mixing Flow

THE EFFECT OF SAMPLE SIZE, TURBULENCE INTENSITY AND THE VELOCITY FIELD ON THE EXPERIMENTAL ACCURACY OF ENSEMBLE AVERAGED PIV MEASUREMENTS

Experimental investigation of flow control devices for the reduction of transonic buffeting on rocket afterbodies

Experiments on the perturbation of a channel flow by a triangular ripple

A PIV Algorithm for Estimating Time-Averaged Velocity Fields

High Reynolds Number Wall Turbulence: Facilities, Measurement Techniques and Challenges

Study of heat transfer enhancement/suppression for molten salt flows in a large diameter circular pipe Part I: Benchmarking

Near Field Measurements of an Axisymmetric Turbulent Jet at Low Reynolds Numbers: A PIV and CTA Comparison

Non-MHD/MHD Experiment under JUPITER-II Collaboration

Turbulence Laboratory

5. 3P PIV Measurements

Towards capturing large scale coherent structures in boundary layers using particle image velocimetry.

PASSIVE CONTROL ON JET MIXING FLOWS BY USING VORTEX GENERATORS

PIV study for the analysis of planar jets in cross-flow at low Reynolds number

The Effect of Endplates on Rectangular Jets of Different Aspect Ratios

Visualization of polymer relaxation in viscoelastic turbulent micro-channel flow

Flow disturbance due to presence of the vane anemometer

Micrometer and Nanometer Spatial Resolution with µpiv

Density Field Measurement by Digital Laser Speckle Photography

Figure 1. Schematic of experimental setup.

DISPERSION IN ROTATING TURBULENCE the development of a 3D-PTV system

PIV Basics: Correlation

PIV optimization for the study of turbulent flow using spectral analysis

Evolution of the pdf of a high Schmidt number passive scalar in a plane wake

Colloquium FLUID DYNAMICS 2013 Institute of Thermomechanics AS CR, v.v.i., Prague, October 23-25, 2013 p.1

ESTIMATING THE FRICTION VELOCITY IN A TURBULENT PLANE WALL JET OVER A TRANSITIONALLY ROUGH SURFACE

The JHU Turbulence Databases (JHTDB)

Flow Characteristics around an Inclined Circular Cylinder with Fin

Generic a-posteriori uncertainty quantification for PIV vector fields by correlation statistics

PARTICLE IMAGE VELOCIMETRY MEASUREMENTS OF STRATIFIED GAS-LIQUID FLOW IN HORIZONTAL AND INCLINED PIPES

Burst-mode laser particle image velocimetry with multi-time step processing for improved dynamic velocity range

Turbulence control in a mixing tank with PIV

PIV measurements and convective heat transfer of an impinging air jet

FLOW VISUALIZATION AND SIMULTANEOUS VELOCITY AND TEMPERATURE MEASUREMENTS IN THE WAKE OF A HEATED CYLINDER

Abstract Particle image velocimetry (PIV)

Design and Aerodynamic Characterization of a Synthetic Jet for Boundary Layer Control

Micro-Flow in a bundle of micro-pillars. A. Keißner, Ch. Brücker

PIV INVESTIGATION OF THE INTERNAL FLOW STRUCTURE IN A CENTRIFUGAL PUMP IMPELLER

PARTICLE IMAGE VELOCIMETRY MEASUREMENTS IN AN AERATED STIRRED TANK

elements remain in high frequency region and sometimes very large spike-shaped peaks appear. So we corrected the PIV time histories by peak cutting an

ANALYSIS OF TURBULENT FLOW IN THE IMPELLER OF A CHEMICAL PUMP

PIV Applications to Thermal Performance of LPG

Effect of Liquid Viscosity on Sloshing in A Rectangular Tank

y * x * Shumpei HARA

Investigation of Heat Transfer in Mini Channels using Planar Laser Induced Fluorescence

Module 3: Velocity Measurement Lecture 16: Validation of PIV with HWA. The Lecture Contains: Hotwire Anemometry. Uncertainity

Instrumentation. Dr. Hui Hu Dr. Rye Waldman. Department of Aerospace Engineering Iowa State University Ames, Iowa 50011, U.S.A

Velocity and temperature measurements in a large-scale Rayleigh-Bénard experiment using LDA and micro thermistors

FLOW CHARACTERIZATION WITHIN A SPHERE-PACKED BED USING PIV MEASUREMENT

Strategy in modelling irregular shaped particle behaviour in confined turbulent flows

INITIAL CONDITION EFFECTS ON KELVIN-HELMHOLTZ INSTABILITIES AND DEVELOPMENT OF A ROUND JET

Internal Flow Measurements of Turbomachinery using PIV

AN UNSTEADY AND TIME-AVERAGED STUDY OF A GROUND VORTEX FLOW

Supporting Online Material for

Multiphase Science and Technology, Vol. 16, Nos. 1-4, pp. 1-20, 2005

Experimental Study of Near Wake Flow Behind a Rectangular Cylinder

Vortex shedding from slender surface mounted pyramids

Journal of Fluid Science and Technology

On the Similarity of Pulsating and Accelerating Turbulent Pipe Flows

Module 3: Velocity Measurement Lecture 15: Processing velocity vectors. The Lecture Contains: Data Analysis from Velocity Vectors

ASSESSMENT OF ANISOTROPY IN THE NEAR FIELD OF A RECTANGULAR TURBULENT JET

PARTICLE MOTION IN WATER-PARTICLE, GAS-PARTICLE AND GAS-DROPLET TWO-PHASE FLOWS

Bubble Sizing by Interferometric Laser Imaging

The Effect of a Uniform Cross-flow on the Circulation of Vortex Rings. E. R. Hassan, R. M. Kelso and P. V. Lanspeary

VORTICITY FIELD EVOLUTION IN A FORCED WAKE. Richard K. Cohn Air Force Research Laboratory Edwards Air Force Base, CA 92524

Intensely swirling turbulent pipe flow downstream of an orifice: the influence of an outlet contraction

2.2 The Turbulent Round Jet

Flow Field Investigation in a Rectangular Shallow Reservoir using UVP, LSPIV and numerical model

Vortex Generator Induced Flow in a High Re Boundary Layer

25 years of PIV development for application in aeronautical test facilities

Dynamics of Large Scale Motions in Bubble-Driven Turbulent Flow

Application of PIV to characterise the Flow- Phenomena of a Heavy-Duty Cylinder Head on a Stationary Flow-Bench

Visualization of Traveling Vortices in the Boundary Layer on a Rotating Disk under Orbital Motion

FLOW MEASUREMENT. INC 102 Fundamental of Instrumentation and Process Control 2/2560

White Paper FINAL REPORT AN EVALUATION OF THE HYDRODYNAMICS MECHANISMS WHICH DRIVE THE PERFORMANCE OF THE WESTFALL STATIC MIXER.

Measurements of Dispersions (turbulent diffusion) Rates and Breaking up of Oil Droplets in Turbulent Flows

Experimental Study on the Effects of Viscosity and Viscoelasticity on a Line Vortex Cavitation

Supplementary Figure 2: One- sided arrangements of transducer. a) flat: 8x8. b) V- shape: 5x6 per side. c) hemispherical cap with 52 transducers.

A NOTE ON THE CONTRIBUTION OF DISPERSIVE FLUXES TO MOMENTUM TRANSFER WITHIN CANOPIES. Research Note

Visualization and LASER measurements on flow field and sand movement on sand dune

Experimental study of the oscillatory interaction between two free opposed turbulent round jets

PIV STUDY OF LONGITUDINAL VORTICES IN A TURBULENT BOUNDARY LAYER FLOW

Investigation of the development of streamwise vortices from vortex generators in APG separation control using PIV

PIV Measurements of the Influence of Seeding Particles Concentration on the Velocity of an EHD Flow

Measuring Particle Velocity Distribution in Circulating Fluidized Bed

Signal-to-noise ratio, error and uncertainty of PIV measurement

Applied Fluid Mechanics

3.3 Quantitative Image Velocimetry Techniques

Investigation of Particle Sampling Bias in the Shear Flow Field Downstream of a Backward Facing Step

Full-field pressure from 3D PIV snapshots in convective turbulent flow

ON THE ACCURACY OF SCALAR DISSIPATION MEASUREMENTS BY LASER RAYLEIGH SCATERING.

Endoscopic PIV in a helical pipe coil

PIV Validation of Numerical Models for Turbulent Flows in a Water Test Section for Liquid Metal Target

Quantitative Measurement of planar Droplet Sauter Mean Diameter in sprays using Planar Droplet Sizing

PASSIVE SCALAR MIXING IN A TURBULENT JET

Visualization of Xe and Sn Atoms Generated from Laser-Produced Plasma for EUV Light Source

Experimental Study on the Non-reacting Flowfield of a Low Swirl Burner

TRACKING OF THERMAL STRUCTURES FROM INFRARED CAMERA BY PIV METHOD

Transcription:

Multiple-eye PIV Eisaku Atsumi 1, Jun Sakakibara 2,* 1: Graduate School of Science and Technology, Meji university 2: Department of Mechanical Engineering, Meji university * Correspondent author: sakakiba@meiji.ac.jp Keywords: PIV, accuracy, dynamic-range, microlens array ABSTRACT This paper describes the new method of PIV to reduce error associated with measurement of particle displacement by computing ensemble average of n=7 sub-images projected on a single image sensor through microlenses. Stereo PIV method was applied to evaluate instantaneous velocities based on combinations of sub-images, and its ensemble average was computed at each instance. The system was applied to a fully developed pipe flow, and statistics were compared to DNS results. The random errors, estimated from the discrepancy of the measured rms velocity to the DNS, was successfully reduced by a factor of 1 n. 1. Introduction Typical velocity dynamic range of particle image velocimetry (PIV) is approximately 1:100 (Adrian 2005), which is far below conventional velocimeter such as hot-wire anemometry or laser Doppler velocimetry. This limitation mainly comes from error associated with measurement of particle displacement, which is typically 0.1 pixels. Further reduction of such error can be achieved by a method called pyramid correlation (Sciacchitano et al. 2012), which uses linear combination of the correlation functions computed at different time intervals. Evaluation of ensemble averaged correlation functions reduces random error of particle displacement by a factor 3. While pyramid correlation uses ensemble average of correlation functions computed from temporal series of images, we propose an alternative way that computes ensemble average of particle displacements measured by multiple cameras viewing simultaneously from different directions. If the random error involved in particle displacements evaluated from images of each camera are mutually independent, the random error in the ensemble average of them reduces n, where n is the number of cameras, according to central -1/2 limit theorem. In this paper, we describe a PIV system having optical equipment named multiple-eye camera, which captures the images viewing from multiple directions. Stereo PIV method was applied to evaluate instantaneous velocities based on combinations of images captured by each eye, and its ensemble average was computed at each instance. Application of this system to a turbulent pipe flow demonstrated the reduction of the random errors in the velocity signals.

2. Method 2.1 Optical design of multiple-eye camera Optical configuration of the multiple-eye camera is shown in Fig.1. First, the ray of light from objects is concentrated by an objective lens, and then the ray is collimated and expanded by a collimator lens and beam expander. Finally, the ray is focused on a C-MOS image sensor (Fastcam SA3, 1024x1024 pixels, pixel size 17x17µm, Photron) through micro lens array. By this 2 configuration, each micro-lens projects a same object, but viewing from slightly different direction, on the image sensor. An image projected by a single micro-lens is hereafter referred sub-image. An iris installed between the objective lens and collimator lens eliminate the overlap of adjacent sub-images on the sensor. The sub-image has a dimension of 2 mm in diameter on the sensor and corresponding diameter in the object plane is 4 mm. Total of 25 sub-images are projected. A snapshot of actual camera is shown in Fig.2. Fig. 1 Optical design of multiple-eye camera.

Fig. 2 Snapshot of multiple-eye camera. From the left, the camera consist of objective lens (85mm F1.4 EX DG HSM, Sigma), collimator lens (50mm Dia., 0.66 NA, Uncoated, Calibration Grade Aspheric Lens, Edmund Optics),plane concave lens (SLB-50-80NM, Sigma Koki),plane convex lens (SLB-50-100PM,Sigma Koki) and microlens array (Fly-eye-lens 730, Koyo,focal length 10mm). 2.2 Flow apparatus and instruments Fig.3 and Fig.4 show schematic of flow apparatus and instruments. Water pumped by an centrifugal pump (MDH-401SE5-D, 200/200-12.0L/min-m, 0.75kW, Iwaki) flows through a circular pipeline. This pipeline has straight section of Plexiglass circular pipe having diameter of D(=2R)=50 mm and length of L=123D. The pipe was surrounded by a Plexiglas rectangular container filled with water, i.e., a water jacket, to minimize the distortion of the image observed across the round surface of the pipe. Tracer particles (Silvercoat hollow sphere, 10µm, Dantec) was seeded in the water. The temperature of water was maintained at 20 ± 0.1! C by use of a heat excahger and a chiller (RKS750F, 1.97kW, Orion) controlled by a digital temperature controller (E5CN, Omron). Cartesian coordinate system has been applied with its origin set at the center of the circular cross-section of the pipe at the inlet of the straight section. The axes x is streamwise, y is vertical and z is perpendicular to both x and y. Velocity components along x, y and z directions are represented by u,v and w, respectively. Bulk mean velocity Ub of the pipe flow was 1.065m/s based on electromagnetic flowmeter (AXF050G, Yokogawa), and corresponding Reynold s number was Re= UbD/ν=4.86 x 10 4, where ν is kinematic viscosity. A test section was located at x=84d where the flow reaches fully-develped turbulent. A laser light sheet created by single cavity Nd-YLF laser with double-pulse option (DM-10, 10 mj/pulse, Photonics Industries) with a laser light sheet optics illuminated a planar volume parallel to x-y plane through z=0. Time interval between double pulses of the laser was varied in a range from Δt=30 µs to 500 µs, and particles illuminated by each pulses were exposed onto two

successive image frames by use of a delay pulse generator (9600, Quantum Composers). The frame rate of the camera was set at 125Hz, and corresponding data rate of PIV output was 62.5Hz. Fig. 3 Schematic of the pipe flow facility. Fig. 4 Schematic of the PIV setup. 2.3 Stereo PIV and calibration Since the viewing direction for different sub-image is not identical, in-plane particle displacement computed from individual sub-image does not coincide if non-zero out-of-plane displacement exists. This implies that the stereo-piv method can be applied to extract whole

three-components of velocity vector based on any combination of two different sub images. Here, we define the i-th component of velocity vector evaluated from a combination of j- and k-th sub-image taken at coordinate x and time t as v i, j, k ( x, t), named hereafter as elementary velocity. Interrogation window size was 50 x 50 pixels, which corresponds to 2.2 x 2.2 mm in object 2 plane. Direct cross-correlation of images in interrogation window of the first frame and search area in the second frame was computed to evaluate two component displacement vectors of the particles, and whole three-component velocity vector was estimated by stereo PIV algorithm (Sakakibara et al. 2004). Since the stereo-piv requires precise image calibration, a calibration plate, where a regular grid of markers of 0.3mm in diameter and 0.6mm interval was printed in terms of laser marking technology, was placed on the light sheet plane with a slight angle respect to the x direction. Calibration image was captured at two different locations of the plate, i.e. the distance between the locations were set at 2 mm, which was achieved by shifting the plate in x direction. Displacement of particle, which travels at U b in x direction, in the image plane is summerised in Table 1. Δt [µs] particle displacement [pixel] 30 0.7252 60 1.4504 125 3.0216 250 6.0432 500 12.0864 Table 1 Displacement of particle travels at bulk velocity. 2.4 Ensemble average of elementary velocities After evaluating elementary velocities based on all combination of sub-images, its ensemble average, named hereafter as ensemble-averaged velocity is calculated by n n v~ 1 i ( x, t) = vi, j, k ( x, t) nc2 j= 1, k= j+ 1 (1) where n refers number of sub-images used. 3. Result and discussion 3.1 Image of particles and calibration plate

Fig.5 shows a raw image of the calibration plate captured by this system. The image involves 7 sub-images, which is perfectly in round shape, surrounded by another 23 sub-images that has some deficit in its shape. Here we use the perfectly-round sub-images (n=7) to compute elementary velocities and other defected sub-images are masked out. Fig.6 shows particle image after applying the mask. Typical particle image size was approximately 5 pixels. Fig. 5 Raw image of calibration plate. Image size is 512x512 pixels. Fig. 6 An example of raw particle image. Image mask was applied to eliminate defected subimages. Contrast was adjusted for clarity. 3.2 Temporal development of instantaneous velocity Fig.7 shows temporal series of instantaneous elementary and ensemble-averaged velocity measured at y=0 with two different Δt. Elementary velocities represented by blue marker were all scattered around ensemble-averaged velocity indicated by black solid line. The scattering of elementary velocity at each instant reflects purely random error of each elementary velocity, while fluctuation of the ensemble-average velocity reflects both random error and actual fluctuation of velocity due to turbulent motion of the flow. Standard deviation of elementary and ensemble-averaged velocity indicated respectively by green and red dashed lines shows significant difference of amplitude of the signals at Δt=30µs. Here the typical particle mean displacement is 0.7 pixels referring Table.1, which is comparable in order of magnitude to the subpixel random error, ~0.1 pixels, of the particle displacement. Note that rms of out-of-plane w component is significantly larger than that of in-plane v component. By symmetry, both standard deviations should be equal, but the error of out-of-plane component evaluated by stereo PIV algorithm might be augmented by use of narrow angle, such as 7 degrees, of the view axis of two sub-images. In contrast to Δt=30µs, difference of rms of elementary and ensemble-average velocity is reduced at Δt=500µs, where the random error of the elementary velocity is relatively

small compared to the larger particle mean displacement such as 12 pixels. Significant error of the out-of-plane component is still observed in Δt=500µs. (a) Δ t=30µs (b) Δ t=500µs Fig. 7 Temporal series of instantaneous u, v and w components of velocity measured at the center of the pipe. Symbol and solid line indicates elementary and ensemble-averaged velocity,

respectively. Black and green dash indicates mean and standard deviation of ensemble-averaged velocity, and red dash indicates standard deviation of elementary velocities at each instance. 3.3 Mean and RMS velocity Fig.8 shows radial distribution of streamwise mean velocity U + calculated from ensembleaveraged velocity, where superscript denotes the velocity and length being normalized by friction velocity uτ and viscous wall unit ν u, respectively. The friction velocity was estimated τ based on Blasius friction formula (Schlichting 1979). As a reference, a DNS result obtained at Re=44000 by Wu & Moin (2008) is overlaid in a dashed line. The value under Δt 60 µs have agreement with the DNS results, while Δt=30 µs is overestimated. Mean velocity does not affected theoretically by pure random error in the measured velocity, but it is sensitive to bias error such as peak-locking, which is a tendency of the measured particle displacement to be biased towards integer pixel values. Maximum bias error in measured mean velocity increases as decreasing Δt by Angele & Muhammad-Klingmann (2005) due to the peak-locking. Discrepancy of measured value to the DNS arising in a case of short Δt is also found in radial profile of RMS velocity profiles shown in Fig.9. Both u + rms and v + rms under the case of Δt=250 µs and 500µs shows good agreement with the DNS, while other cases having smaller Δt shows larger discrepancy, which was observed in instantaneous velocity shown in Fig.7. Fig. 8 Streamwise mean velocity profile.

(a) 1 y R (b) Fig. 9 RMS velocity profile; (a) streamwise component; (b) radial component. 3.4 Estimation of random error associated with particle displacement

By assuming that the DNS result always indicates true value, the discrepancy found in Fig.9 might give an estimate of magnitude of random error of velocity measurement. The measured rms value of the streamwise velocity without normalization, u rms, measured, can be expressed in terms of squared-sum of true value of rms displacement of particles in image plane and random error, ε, associated with estimation of particle displacement in the image plane by a relationship; u rms measured = + 2 2 2 {( urms DNS uτ Δt α x ) + ε } 1, α Δt,. (3) Here α represents the physical particle displacement in the object plane corresponding to a particle displacement of one pixel in image plane. The α has been known through the calibration procedure. Note that the error in Δt and α was so small that their contribution was neglected in (3). Furthermore this formula does not account for the reduction of random error due to the lack of spatial resolution, which acts like low pass filter. The error ε obtained from (3) is plotted against n in Fig.10. In this figure, the ε estimated from u + rms agreeing with that of DNS, i.e. the case of Δt 250 µs, were eliminated. Also ε being complex value is not plotted. The markers at n=2 (n=7) are the ε evaluated from elementary velocity (ensemble-averaged velocity). At a glance, the error ε decays as increasing n. Based on central limit theorem, the random error of ensembleaveraged velocity is expected to be proportional to 1 n, if the all of the elementary velocities are mutually independent. This is evident in Fig.10, where the data agree with solid curves expressed by Here εn= 2 n=2 2 ε = ε. (4) n denotes ensemble average of ε estimated from elementary velocities, which was evaluated from n=2 sub-images, at specific Δt. In other words, the solid lines were drawn through the mean error of elementary velocities (n=2). It is clear that the error ε decays proportionally to 1 n, and that implies the all elementary velocities are mutually independent.

(a)1-y/r=1 (b)1-y/r=0.2 Fig. 10 Estimated random error of streamwise component of particle displacement vector. Type of symbols are all identical to that of Fig. 9.

4. Conclusion We developed a new PIV system, named multiple-eye PIV, which reduces error associated with measurement of particle displacement by computing an ensemble average of velocities evaluated from n=7 sub-images captured on a single image sensor through micro-lens array. The system was applied to a fully developed pipe flow, and mean and rms velocity profiles were compared to that of DNS. The random errors were estimated from the discrepancy of the measured rms velocity to the DNS. The random error in the ensemble-averaged velocity was successfully reduced by a factor of consequently reduction of the error, is a challenge for the future. 1 n. Further refinement of imaging optics to increase n, and 5. Reference o Adrian RJ (2005) Twenty years of particle image velocimetry. Exp Fluids 39:159-160. o Angele KP, Muhammad-Klingmann B (2005) A simple model for the effect of peak-locking on the accuracy of boundary layer turbulence statistics in digital PIV. Exp Fluids 38: 341-347. o Sakakibara J, Nakagawa M, Yoshida M (2004) Stereo-PIV study of flow around a maneuvering fish. Exp Fluids 36:282-293. o Schlichting H (1979) Boundary-layer theory. McGraw-hill. o Sciacchitano S, Scarano F, Wieneke B (2012) Multi-frame pyramid correlation for timeresolved PIV. Exp Fluids 53:1087-1105. o Wu X, Moin P (2008) A direct numerical simulation study on the mean velocity characteristics in turbulent pipe flow. J Fluid Mech 608:81-112.