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
Link To Document