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FIBRE OPTIC AND CAPACITANCE PROBES IN TURBULENT FLUIDIZED BEDS
Authors:H I Farag  T Mejdell  K Hjarbo  P Ege  M Lysberg  A GRISLING   s  H De Lasa
Affiliation:  a Department of Chemical Engineering, The University of Trondheim, The Norwegian Institute of Technology, Trondheim, Norway b SINTEF Applied Chemistry, Chemical Engineering Section, Trondheim, Norway c Norsk Hydro Research Centre Porsgrunn, Porsgrunn, Norway d Department of Chemical Engineering, Chemical Reactor Engineering Centre, The University of Western Ontario, London, Ontario, Canada
Abstract:In the present study, local flow properties are investigated in pilot plant scale fluidized bed reactors using both fibre optic and capacitances probes. Measurements are conducted at ambient as well as at 150°C. The system used is air and spent FCC particles (mean particle diameter: 65pm). The static bed height is 1.6 m. Bubbling and turbulent regimes (V = 0.40 and 0.70 m/s) are investigated in two 0.3 and 0.5 m ID columns.

Bubble fraction under the bubbling regime and at room temperature, measured using fibre optic and capacitance probes, are in good agreement. However, in the turbulent regime, fibre optic probes are prone to underestimate the bubble fraction while capacitance sensors tend to overestimate it. These discrepancies between fibre optic and capacitance measurements increase with temperature.

Using capacitance probes, a prevalent flat bubble rise velocity profile is measured. This is assigned to the relatively slow response, to the size and to the geometry of the capacitance probes. Overall this gives an underestimation of the bubble frequency and an overestimation of the bubble contact time and the bubble contact length.

Due to the high fibre optic probe sensitivity, care should be taken in the interpretation of signals. Overestimation of bubble frequency leads to underestimation of both bubble contact times and bubble contact lengths.
Keywords:Turbulent fluidization  capacitance probe  optic probe
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