Abstract
This study investigates the complex spatial characteristics of a gas-solid dense-phase fluidized bed for a separation system. A custom-designed perspex bed, equipped with multi small holes and different distributors, was used to explore gas-solid suspension characteristics. The results show that there is a certain spatial heterogeneity in the density of the gas-solid separation fluidized bed. The spatial heterogeneity of gas-solid fluidized beds is characterized by global and local dependence. An empirical model that predicts the relative solid mass flow rate was proposed. GeoDetector technology (including a factor detector, interaction detector, risk detector, and ecological detector) was first introduced to quantify the spatial characteristics of a gas-solid fluidized bed. The influence of each factor on the spatial heterogeneity of particle solid mass flow rate follows the order: axial position > gas velocity > radial position > air distributor. The interactive relationship between variables on the spatial characteristics of gas-solid separation fluidization shows a nonlinear enhancement.
Graphical Abstract
GeoDetector was used to reveal the dominant factor in a gas-solid fluidized bed.
Gas-solid fluidized has global and local dependence on spatial heterogeneity.
An empirical model that predicts the relative solid mass flow rate is proposed.
The axial position has a direct effect on the spatial heterogeneity in the bed.
HIGHLIGHTS
Disclosure statement
No potential conflict of interest was reported by the author(s).