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- The Fluidized Bed Reactor
- (503b) The Axial Solids Hold-up Profile in the Riser of a Cfb
In order to define the transition between the dilute and S-shaped profile, solids hold-up profiles were measured at combined (U,G)-values. The zone of recycling bed material from the L-valve was moreover investigated using the PEPT-technique with 18F-labelled tracers.
Experimental data will be illustrated and correlated together with literature data. The transition from dilute to S-shaped profile is obtained at G > 3.9 U1.8.
The recycle loop can impose a high pressure drop on the riser, even at small G-values. In order to satisfy the pressure balance of the CFB, an S-shaped profile has to exist even at small values of G. This effect of the re-entry zone was measured by PEPT and expressed in an acceleration length, i.e. the height above the L-valve needed by the particle to achieve its stable particle velocity. Results are again Expressed as height vs. (U,G), and compared with a theoretical model to predict the acceleration zone. Experimental and model results are in very good agreement. In general, the re-entering particles will spend a time less than 5 to 7.5 % of their residence time in the riser, hence without major importance for calculating conversions in function of this residence time.
Literature data moreover enable us to define the transition between the S-shaped and dense profiles, obtained at G > 11 U1.8.
The simple equations proposed by the research prove of better accuracy than the more complicated correlations found in literature.
*Corresponding author: Professor Jan Baejens; e-mail: J.Baejens@bham.ac.uk; tel. +44 121 4145343; fax. +44 121 414 5323