Article ID Journal Published Year Pages File Type
652189 Experimental Thermal and Fluid Science 2012 8 Pages PDF
Abstract

This study presents the results of an experimental investigation of the hydrodynamics of conical spouted beds operating with high density particles. This type of spouted beds is frequently encountered in chemical vapor deposition coating of nuclear fuel elements. Measurements were performed in three 15 cm ID full circular (γ = 30°, 45°, 60°) and one half circular conical spouted (γ = 30°) bed with yttria-stabilized zirconia particles (dp = 0.5, 1 mm; ρp = 6050 kg/m3). For the complete characterization of the hydrodynamic regimes, simultaneous high speed camera and bed pressure drop measurements were carried out in a half circular conical spouted bed to visualize the gas–solid flow patterns and match them with the corresponding bed pressure drop values and its spectral characteristics. The results show that the minimum spouting velocity increases with cone angle, particle diameter and static bed height. The average bed pressure drop decreases with cone angle. Minimum spouting velocity values obtained from full and half bed experiments resulted in a maximum 15% difference. The spectral analyses of the bed pressure drop indicated a dominant frequency of 12 Hz in the stable spouting region. After the initiation of external spouting, an unstable intermittent spouting region which extends up to approximately 1.2Ums has been identified. The results of this work can be successfully used in the hydrodynamic design of spouted bed nuclear fuel coaters.

► Investigation of conical spouted bed nuclear fuel coaters at cold bed conditions. ► First comprehensive study in a spouted bed of this scale with heavy particles. ► Minimum spouting velocity increases with cone angle, particle diameter, bed height. ► Bed pressure drop decreases with cone angle. ► Results can be successfully used in the design of spouted bed nuclear fuel coaters.

Related Topics
Physical Sciences and Engineering Chemical Engineering Fluid Flow and Transfer Processes
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