Comparison of Particle Image Velocimetry and Laser Doppler Anemometry measurement methods applied to the oil–water flow in horizontal pipe

Abstract In this work, a comparison of Particle Image Velocimetry (PIV) and Laser Doppler Anemometry (LDA) measurement methods was made applied to oil–water two-phase flow in a horizontal pipe. The experiments were conducted in a 15 m long, 56 mm diameter stainless steel pipe using Exxsol D60 oil (density 790 kg/m 3 and viscosity 1.64 mPa s) and water (density 996 kg/m 3 and viscosity 1.0 mPa s) as test fluids. The experiments were performed at different mixture velocities and water cuts. Mixture velocity and water cut vary up to 1.06 m/s and 0.75, respectively. The instantaneous local velocities were measured using PIV and LDA, and based on the instantaneous local velocities mean velocities and turbulence profiles are estimated. The measurements are performed in the vertical plane through the pipe center. A double-pulsed Nd:yttrium aluminium garnet (YAG) laser and a high-speed camera with 1260×1024 px resolution (1.3 Mpx) were used for the PIV measurements. The LDA set-up is a two-colour backscatter system with 3 W Argon-Ion Laser. The time averaged cross-sectional distributions of oil and water phases were measured with a traversable gamma densitometer. The measured mean axial velocity and turbulence profiles using PIV were observed to compare favourably well with LDA measurements. Nevertheless, the PIV measurements are more sensitive for optical disturbances in the dispersed region close to the oil–water interface. Hence, this region cannot be confidently analyzed using PIV, whereas LDA offers full-field measurements even at higher mixture velocities.

[1]  J. Whitelaw,et al.  Convective heat and mass transfer , 1966 .

[2]  L. Drain The Laser Doppler Technique , 1980 .

[3]  Arne Valle,et al.  PRESSURE DROP, FLOW PATTERN AND SLIP FOR TWO PHASE CRUDE OIL/WATER FLOW: EXPERIMENTS AND MODEL PREDICTIONS , 1997 .

[4]  Y. Yeh,et al.  Localized fluid flow measurements with an He-Ne laser spectrometer , 1964 .

[5]  Yassin A. Hassan,et al.  SIMULTANEOUS VELOCITY MEASUREMENTS OF BOTH COMPONENTS OF A TWO-PHASE FLOW USING PARTICLE IMAGE VELOCIMETRY , 1992 .

[6]  Masahiro Kawaji,et al.  Liquid turbulence structure at a sheared and wavy gas-liquid interface , 1997 .

[7]  Panagiota Angeli,et al.  Droplet size and velocity profiles in liquid–liquid horizontal flows , 2004 .

[8]  C. A. Coulaloglou,et al.  Alpha-omega and beyond industrial view of gas/liquid/solid reactor development , 1992 .

[9]  James P. Brill,et al.  A Study of Oil-Water Flow Patterns in Horizontal Pipes , 1996 .

[10]  Liang-Shih Fan,et al.  Particle image velocimetry for characterizing the flow structure in three-dimensional gas-liquid-solid fluidized beds , 1992 .

[11]  F. Durst,et al.  LDA measurements in the near-wall region of a turbulent pipe flow , 1995, Journal of Fluid Mechanics.

[12]  A. Melling,et al.  Principles and practice of laser-Doppler anemometry , 1976 .

[13]  Ronald Adrian,et al.  High resolution measurement of turbulent structure in a channel with particle image velocimetry , 1991 .

[14]  Gerald L. Morrison,et al.  Doppler global velocimetry: problems and pitfalls , 1995 .

[15]  Panagiota Angeli,et al.  Pressure gradient in horizontal liquid-liquid flows , 1999 .

[16]  P. R. Bevington,et al.  Data Reduction and Error Analysis for the Physical Sciences , 1969 .

[17]  Mihail C. Roco,et al.  Particulate two-phase flow , 1993 .

[18]  Oscar Mauricio Hernandez Rodriguez,et al.  Experimental study on oil–water flow in horizontal and slightly inclined pipes , 2006 .

[19]  R. Meynart,et al.  Full-field laser metrology for fluid velocity measurement , 1988 .