Abstract

Low-frequency flow pulsations were utilized to improve the hydrodynamics of the fluidized bed of hydrophilic ultrafine nanosilica powder with strong agglomeration behavior. A gradual fluidization of unassisted fluidized bed through stepwise velocity change was carried out over a wide range of velocities followed by a gradual defluidization process. Bed dynamics in different regions of the fluidized bed were carefully monitored using fast and sensitive pressure transducers. Next, 0.05-Hz square-wave flow pulsation was introduced, and the fluidization behavior of the pulsed fluidized bed was rigorously characterized to delineate its effect on the bed hydrodynamics by comparing it with one of the unassisted fluidized bed. Flow pulsations caused a substantial decrease in minimum fluidization velocity and effective agglomerate diameter. The frequencies and amplitudes of various events in different fluidized bed regions were determined by performing frequency domain analysis on real-time bed transient data. The pulsations and their effects promoted deagglomeration and improved homogeneity of the pulsed fluidized bed.

Highlights

  • Ultrafine nanopowders have attracted considerable attention from various scientific and technological fields owing to their unique properties, which mainly arise from their nanoscale dimensions and extremely high specific surface areas

  • Fine and ultrafine powders, notwithstanding their high surface areas, are often cohesive in nature and difficult to fluidize, making their hydrodynamics poorly understood. This fact was recognized by Geldart [5], who classified particles in different groups based on their fluidization behavior

  • Feur rinthcerreainsecrienasveeilnocviteyloacfitteyratfhteerftuhlel flfuulildfliuzaidtiioznatoiofnthe of tbheedbceadusceadusaeddeacrdeeacsreeiansethine pthreespsurersesdurroepdfrroopmfr5o0m0 s50to0 1s0t0o01s0.0T0hsi.sTphhisenpohmeneonmonenwoanswcaaussceadubseydthe byutphwe aurpdwmairgdramtioignraotfiosonmoef ssoolmides tshoaltidwsetrheaitniwtiaelrley ipnrietsiaelnlyt inprtehseencetnitnratlhreegcieonntroaflthreegfliounidoizfetdhbeed fludiduiezetdo btheed edxupeatnostihoeneoxfptahnesbioend.ofTthhee pbereds.sTuhree pdrreospsureremdarionpedrermelaaitniveedlyreclaotnivstealyntcoatnshtiagnht vatelhoicgihties velforocimtie1s0f0r0oms to10104000s stobe1c4a0u0sse btheecauupswe athrde umpigwraartdionmoigfrsaotliiodns ofrfosmoltidhes fcreonmtratlhreegceionntrwalarsergeiponlenwisahsed repblyentihseheindpbuyt othf ethienpmuatsos ffrtohme mthaesslofwroemr rethgeiolnoswoefrthreegbioends, wofhtihche wbeads,flwuhidicihzewd alassftlubiedciazuesde loafstthe becparuesseenocfethofe lparrgeseeangcgeloofmlaerrgateeas.gglomerates. Another feature of the unassisted fluidization is the occurrence of high frequency fluctuations, which tend to increase with velocity in the later stages of the fluidization cycle and early stages of the defluidization cycle

Read more

Summary

Introduction

Ultrafine nanopowders have attracted considerable attention from various scientific and technological fields owing to their unique properties, which mainly arise from their nanoscale dimensions and extremely high specific surface areas. Fine and ultrafine powders, notwithstanding their high surface areas, are often cohesive in nature and difficult to fluidize, making their hydrodynamics poorly understood This fact was recognized by Geldart [5], who classified particles in different groups based on their fluidization behavior. Group C particles possess high surface area, their applications in processing using gas–solid fluidization remains challenging because of interparticle forces that render their hydrodynamics unpredictable This issue has attracted significant attention in the literature. The hydrodynamics of the fluidized bed of a hydrophilic ultrafine nanopowder subjected to low-frequency flow pulsation was comprehensively investigated in the present work. Towards this end, we first carefully examined the hydrodynamics of the conventional fluidized bed. The influence of pulsation on fluidized bed hydrodynamics was explored through the rigorous analyses of bed dynamics in the frequency domain

Experimental
Mean Pressure Drop
Mean Effective Agglomerate Diameter
Findings
Conclusions
Full Text
Published version (Free)

Talk to us

Join us for a 30 min session where you can share your feedback and ask us any queries you have

Schedule a call