• Title of article

    Prediction of bubble behaviour in fluidised beds based on solid motion and flow structure

  • Author/Authors

    Fan، Xianfeng نويسنده , , Parker، David J. نويسنده , , Yang، Zhufang نويسنده , , Armstrong، Brian نويسنده ,

  • Issue Information
    روزنامه با شماره پیاپی 1 سال 2008
  • Pages
    12
  • From page
    358
  • To page
    369
  • Abstract
    It has been demonstrated that the non-intrusive positron emission particle tracking (PEPT) could be a potential technique for observing bubble flow pattern, measuring bubble size and rise velocity in bubbling fluidised beds according to the solid motion in bubble and its wake. The results indicate that the behaviour of air bubbles varies greatly with the bed materials and superficial gas velocity. Three types of bubbling patterns (namely A, B and C) have been reported in this study, in which the pattern C is observed when the polyethylene fluidised bed is operated at the superficial gas velocity (U−Umf) of 0.25–0.5 m/s and the ratio of bed height to bed diameter is unity. After the comparison of the results measured by the PEPT technique with the values calculated by using a number of empirical correlations, two modified correlations are recommended to calculate the bubble size based on the PEPT data.
  • Keywords
    Fluidisation , Bubble size , Bubble velocity , Bubbling pattern , flow structure
  • Journal title
    Chemical Engineering Journal
  • Serial Year
    2008
  • Journal title
    Chemical Engineering Journal
  • Record number

    122522