Stirrer design for improving fluidization of cohesive powder
A time-resolved X-ray study
Kaiqiao Wu (Guangdong University of Technology, TU Delft - ChemE/Product and Process Engineering)
R. Kamphorst (TU Delft - ChemE/Product and Process Engineering)
A.M.T. Bakker (TU Delft - BT/Industriele Microbiologie)
Jasper Ford (Student TU Delft)
Evert Wagner (TU Delft - ChemE/O&O groep)
Olga Ochkin-Koenig (BASF SE)
Miika Franck (BASF SE)
Dominik Weis (BASF SE)
Gabrie M.H. Meesters (TU Delft - ChemE/Product and Process Engineering)
J. Ruud Van Ommen (TU Delft - ChemE/Product and Process Engineering)
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Abstract
Stirring has been recognized in the literature as a promising technique for facilitating fluidization of cohesive powders, via inputting additional energy to counteract interparticle forces. However, the influence of operating conditions and stirrer configurations on flow behavior remains largely unknown, which impedes the practical implementation of stirred fluidization. Utilizing X-ray imaging, this research demonstrates that stirring enhances fluidization in cohesive micron-silica powder (Sauter mean diameter [Formula presented]) by collapsing the powder packing structure, and transitioning channeling beds into bubbling states. Comb-like configurations featuring fewer stirrers and blades, placed in the bottom region, have shown to be highly effective. Excessive stirring can lead to air pockets and a compacted phase of particles on the column walls, undermining the interaction between particles and stirrers. Additionally, the experiments show that maximizing the sweeping coverage, employing complex asymmetrical configurations, and avoiding tortuous gas pathways are preferable.
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