2014
DOI: 10.4236/aces.2014.41002
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On the Influence of Particles Characteristics on Moisture Diffusivity during Drying of Granular Porous Media

Abstract: The objective of this work was to study the diffusive mechanisms of mass transfer predominant in the drying of cylindrical unconsolidated granular porous media of different diameters of porous spherical particles. The experimental study was based on determining the drying kinetics of the porous media evaluated and on obtaining the physical properties regarding the particles that constitute them. Moisture data as a function of time were obtained by subjecting the porous media to an upward single-phase flow of h… Show more

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Cited by 11 publications
(3 citation statements)
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“…In general, smaller particles with broader PSD have higher propensities to form particle− particle bridges. As reported by Freire et al (2014), 23 vapor and liquid diffusion into the cake is regulated by the cake tortuosity and cake porosity properties. When the cake is formed, the PSD plays a major part in defining tortuosity, which is an important contributor to the resistance to gas flow and hence gas velocity and the opportunity for the gas to contact the wet crystal surfaces and remove the residual solvent left from the washing process.…”
Section: Model Validation Experimentsmentioning
confidence: 99%
“…In general, smaller particles with broader PSD have higher propensities to form particle− particle bridges. As reported by Freire et al (2014), 23 vapor and liquid diffusion into the cake is regulated by the cake tortuosity and cake porosity properties. When the cake is formed, the PSD plays a major part in defining tortuosity, which is an important contributor to the resistance to gas flow and hence gas velocity and the opportunity for the gas to contact the wet crystal surfaces and remove the residual solvent left from the washing process.…”
Section: Model Validation Experimentsmentioning
confidence: 99%
“…This can be achieved by using adsorption columns filled with some porous adsorptive material coupled to the dryer fluid supply system [32] . The estimated potential drying energy savings must lie between 25 and 30% of the total energy employed in drying, which can be reached by adopting an adequate drying method, modification of the dryer design, or simply by using other drying operating conditions [27] .…”
Section: Energy Aspectsmentioning
confidence: 99%
“…The movement of fluid in-between micro and nano-size pores is a combination of diffusion and effusion. A few experimental studies have been conducted so far to model diffusioneffusion driven drying in cemented particulate matter [33]. The lack of knowledge is due to improper understanding of the couple effects, and also the unavailability of the coupled partial differential equations to define the problem considering diffusion-effusion coupled with the heat transfer in unsaturated porous media is a limitation in proper modelling with numerical methods [34].…”
Section: Introductionmentioning
confidence: 99%