Effect of vibrational modes on fluidization characteristics and solid distribution of cohesive micro- and nano-silica powders

Journal Article (2024)
Author(s)

R. Kamphorst (TU Delft - ChemE/Product and Process Engineering)

Kaiqiao Wu (TU Delft - ChemE/Product and Process Engineering)

M. van Baarlen (TU Delft - Sanitary Engineering)

GMH Meesters (TU Delft - ChemE/Product and Process Engineering)

Jan Rudolf Van Ommen (TU Delft - ChemE/Product and Process Engineering)

Research Group
ChemE/Product and Process Engineering
Copyright
© 2024 R. Kamphorst, K. Wu, M. van Baarlen, G.M.H. Meesters, J.R. van Ommen
DOI related publication
https://doi.org/10.1016/j.ces.2024.119911
More Info
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Publication Year
2024
Language
English
Copyright
© 2024 R. Kamphorst, K. Wu, M. van Baarlen, G.M.H. Meesters, J.R. van Ommen
Research Group
ChemE/Product and Process Engineering
Volume number
291
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Abstract

In this study, the impact of different vibrational modes on the fluidization characteristics of cohesive micro- and nano-silica powder was examined. Fractional pressure drop, bed expansion measurements, and X-ray imaging were utilized to characterize the fluidization quality. The densities of the emulsion phase at the top and bottom of the column were quantified and compared, providing insights into the solid distribution within the fluidized bed. In the absence of vibration, neither powder could be fluidized within the considered range of superficial gas velocities. Vertical vibration was found to initiate fluidization for both powders. In contrast, elliptical vibration failed to overcome the channelling behavior when fluidizing the micro-powder. For nano-powder, combined channelling and powder compaction occurred when the bed was subjected to elliptical vibration. For the micro-powder, it was observed that bed homogeneity was independent of vertical vibration intensity but improved with increasing superficial gas velocity. For nano-powder, intensifying vertical vibration led to segregation, likely due to agglomerate densification. Furthermore, fractional pressure drop measurements proved to be a strong tool in assessing fluidization quality, providing insights that could not be attained by conventional indicators.