Abstract
A model of granular flow in the regime of a moving bed under conditions of granular phase ablation is developed. The model is based on the well-known two-layer representation of stratified slurry flow, which assumes a dynamic equilibrium between the bottom (granular) layer and the upper layer of solids-liquid suspension. The mass transfer rate from the bottom layer to the upper one is defined on the basis of digestion model for a single spherical lump. The model developed allows estimation of the lengths required for the total digestion of lumps in a moving bed and the axial pressure gradient distribution for different flow regimes.
Cite
CITATION STYLE
Eskin, D., Leonenko, Y., & Vinogradov, O. (2003). Simulation of pipeline slurry flow under conditions of granular phase ablation. Chemical Engineering and Technology, 26(1), 97–102. https://doi.org/10.1002/ceat.200390014
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