期刊文献+

Measuring turbulence in a circulating fluidized bed using PIV techniques 被引量:6

Measuring turbulence in a circulating fluidized bed using PIV techniques
原文传递
导出
摘要 This study utilized the particle image velocimetry (P1V) technique, non-invasively near the wall, in the developing region, for the measurements of laminar and turbulent properties during circulation of Geldart B type particles in the U.S. Department of Energy (DOE) National Energy Technology Laboratory (NETL) riser. A novel method was used to measure axial and radial laminar and turbulent solids dispersion coefficients using autocorrelation technique. The instantaneous and hydrodynamic velocities for the solid phase were measured simultaneously in the axial and radial directions using a CCD camera, with the help of a colored rotating transparency. The measured properties, such as laminar and Reynolds stresses, laminar and turbulent granular tempera- tures, laminar and turbulent dispersion coefficients and energy spectra exhibited anisotropy. The mixing in the riser was on the level of clusters. The total granular temperatures were in reasonable agreement with the literature values. However, the axial and radial solids dispersion coefficients measured near the wall were slightly lower than the radially averaged values in the literature. This study utilized the particle image velocimetry (P1V) technique, non-invasively near the wall, in the developing region, for the measurements of laminar and turbulent properties during circulation of Geldart B type particles in the U.S. Department of Energy (DOE) National Energy Technology Laboratory (NETL) riser. A novel method was used to measure axial and radial laminar and turbulent solids dispersion coefficients using autocorrelation technique. The instantaneous and hydrodynamic velocities for the solid phase were measured simultaneously in the axial and radial directions using a CCD camera, with the help of a colored rotating transparency. The measured properties, such as laminar and Reynolds stresses, laminar and turbulent granular tempera- tures, laminar and turbulent dispersion coefficients and energy spectra exhibited anisotropy. The mixing in the riser was on the level of clusters. The total granular temperatures were in reasonable agreement with the literature values. However, the axial and radial solids dispersion coefficients measured near the wall were slightly lower than the radially averaged values in the literature.
出处 《Particuology》 SCIE EI CAS CSCD 2011年第6期572-588,共17页 颗粒学报(英文版)
基金 support by the U.S. Department of Energy (DOE) University Grant(DE-FG26-06NT42736)
关键词 Particle image velocimetry (PIV) Dispersion coefficient Autocorrelation Turbulence Anisotrnpy Particle image velocimetry (PIV) Dispersion coefficient Autocorrelation Turbulence Anisotrnpy
  • 相关文献

参考文献105

  • 1Ambler, P. A., Milne, B.J., Berruti, F. & Scott, D, S. (1990). Residence time distribution of solids in a circulating fluidized bed: Experimental and modelling studies. Chemical Engineering Science, 45, 2179-2186.
  • 2Arastoopour, H. & Yang, Y. (1992). Experimental studies on dilute gas and cohesive particles flow behavior using laser Doppler anemometer. In O. E. Potter, & D. J. Nicklin (Eds.), Fluidization VI1 (pp. 723-?30).
  • 3NewYork: Engineering Foundation. Avidan, A. & Yerusbalmi, J. ( 1985 ). Solids mixing in an expanded top fluid bed. AIChE Journal, 31,835-841.
  • 4Bader, R., Findlay, J. & Knowlton, T. M. (1988). Gas/solids flow pattern in a 30.5 cm diameter circulating fluidized bed. In P. Basu, & J. F. Large (Eds.), Circulating fluidized bed technology Il (pp. 127-137). Oxford: Pergamon Press.
  • 5Bahary, M. (1994). Experimental and computational studies of hydrodynamics in two and three phasefluidize beds. Unpublished doctoral dissertation, Illinois Institute of Technology, Chicago.
  • 6Bhusarapu, S., AI-Dahhan, M. H. & Dudukovie, M. P. (2006). Solids flow mapping in a gas-solid riser: Mean holdup and velocity fields. Powder Technology, 163, 98-123.
  • 7Bi, H. T,, Ellis, N., Abba, I. A. & Grace,J. R. (2000), A state-of-the-art review of gas-solid turbulent fluidization, Chemical Engineering Science, 55, 4789-4825.
  • 8Breault, R. W, (2006). A review of gas-solid dispersion and mass transfer coefficient correlations in circulating fiuidized beds. Powder Technology, 163, 9-17.
  • 9Breault, R, W., Guenther, C. P. & Shadle, L.J. (2008). Velocity fluctuation interpreta tion in the near wall region of a dense riser. Powder Technology, 182, 137-145.
  • 10Breault, R. W., Ludlow, C.J. & Yue, P, C. (2005). Cluster particle number and granular temperature for cork particles at the wall in the riser ofa CFB. Powder Technology, 149, 68-77.

同被引文献31

引证文献6

二级引证文献33

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部