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IbD PU Deliverable 3.1 particles with the pressure drop across the bed equalized with the weight of the bed. In the study, it was pointed out that the rotating fluid bed combined with centrifugal sludge dewatering would result in further process integration and intensification on a sludge incineration plant. Wong et al. (2000) designed and constructed a small-scale RFB for the investigation of the possibility of incineration of wool scouring sludges. In the cold test, different operating parameters were tested for optimization which were used in the second phase hot test in the experiment to ensure complete fluidization and minimum particle elutriation. In the RFB, the efficient mixing in the turbulent fluid provided a good environment to increase the combustion efficiency even when a maximum moisture up to 70% was present in all sludges. The gas combustion also benefited from the special advantage of swirling flow in the RFB. A more advanced version of the rotating fluidized bed system was developed by Watano et al. (2004) for improving the flowability of cohesive fine powders (Figure 14). The rotating fluidized bed contained a plenum chamber and a porous cylindrical air distributor. A cylindrical metal filter to retain fine powder was equipped inside air distributor. The experiments indicated the novel system could improve the flowability of cohesive fine corn starch. 18PDF Image | Solids handling for intensified process technology
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