Article ID Journal Published Year Pages File Type
237688 Powder Technology 2011 6 Pages PDF
Abstract

A method has been developed to deduce a “breakup” force in a packed bed based on measured pressure drop and internal cavity size hysteresis data in a conical spouted bed. The pressure drop over the vertical jet is estimated by the Eulerian–Eulerian two-fluid model using the commercial Fluent software. The pressure drop over the packed bed is extracted from the measured total pressure drop following a flow rate descending process in the spouted bed, while the “breakup” force is determined from the combination of measured total pressure drop and internal jet height following the flow ascending process, the simulated pressure drop over the gas jet and the pressure drop over the loosely packed upper bed section. Such a proposed method can be applied in the future to develop a generalized expression for the “breakup” force in spouted beds and other packed bed systems where a vertical fluid jet is issued into the packed particles.

Graphical AbstractThe “breakup” force in packed beds is deduced based on measured pressure drop and internal cavity data, which can be applied to develop a generalized expression for the “breakup” force in systems where a vertical jet is issued into packed particles.Figure optionsDownload full-size imageDownload as PowerPoint slide

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Physical Sciences and Engineering Chemical Engineering Chemical Engineering (General)
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