TY - JOUR
T1 - Lagrangian velocity and acceleration statistics of fluid and inertial particles measured in pipe flow with 3D particle tracking velocimetry
AU - Oliveira, J.L.G.
AU - van der Geld, C.W.M.
AU - Kuerten, J.G.M.
N1 - Funding Information:
The authors gratefully acknowledge support of this work by Brazilian National Council of Research (CNPq) through the project call “Science without borders”, protocol number: Proc. 405700/2013-0. Special thanks to Prof. Júlio César Passos from UFSC/Brazil and Dr. Coen Baltis from Eindhoven University of Technology. The authors are indebted to Prof. Borée from ENSMA/France for his valuable comments.
Publisher Copyright:
© 2015 Elsevier Ltd.
PY - 2015/7/1
Y1 - 2015/7/1
N2 - Three-dimensional particle tracking velocimetry (3D-PTV) has been applied to particle-laden pipe flow at Reynolds number 10,300, based on the bulk velocity and the pipe diameter. The volume fraction of the inertial particles was equal to 1.4×10-5. Lagrangian velocity and acceleration statistics were determined both for tracers and for inertial particles with Stokes number equal to 2.3, based on the particle relaxation time and the viscous time scale. The decay of Lagrangian velocity and acceleration correlation functions was measured both for the fluid and for the dispersed phase at various radial positions. The decay of Lagrangian velocity correlations is faster for inertial particles than for flow tracers, whereas the decay of Lagrangian acceleration correlations is about 25% slower for inertial particles than for flow tracers. Further differences between inertial and tracer particles are found in velocity fluctuations evaluated for both positive and negative time lags. The asymmetry in time of velocity cross-correlations is more pronounced for inertial particles. Quadrant analysis revealed another difference still near the wall: ejection and sweep events are less frequent for inertial particles than for tracers.
AB - Three-dimensional particle tracking velocimetry (3D-PTV) has been applied to particle-laden pipe flow at Reynolds number 10,300, based on the bulk velocity and the pipe diameter. The volume fraction of the inertial particles was equal to 1.4×10-5. Lagrangian velocity and acceleration statistics were determined both for tracers and for inertial particles with Stokes number equal to 2.3, based on the particle relaxation time and the viscous time scale. The decay of Lagrangian velocity and acceleration correlation functions was measured both for the fluid and for the dispersed phase at various radial positions. The decay of Lagrangian velocity correlations is faster for inertial particles than for flow tracers, whereas the decay of Lagrangian acceleration correlations is about 25% slower for inertial particles than for flow tracers. Further differences between inertial and tracer particles are found in velocity fluctuations evaluated for both positive and negative time lags. The asymmetry in time of velocity cross-correlations is more pronounced for inertial particles. Quadrant analysis revealed another difference still near the wall: ejection and sweep events are less frequent for inertial particles than for tracers.
KW - 3D particle tracking velocimetry
KW - Acceleration statistics
KW - Inertial particles
KW - Turbulence
KW - n/a OA procedure
UR - http://www.scopus.com/inward/record.url?scp=84926226711&partnerID=8YFLogxK
U2 - 10.1016/j.ijmultiphaseflow.2015.03.017
DO - 10.1016/j.ijmultiphaseflow.2015.03.017
M3 - Article
VL - 73
SP - 97
EP - 107
JO - International journal of multiphase flow
JF - International journal of multiphase flow
SN - 0301-9322
ER -