Drag force is a key parameter in the numerical modeling of gas-particle flow in circulating fluidized beds. The reliability of current drag force correlations over the regime of fast fluidization has, however, not been thoroughly investigated. In this article, a drag force correlation accounting for the clustering effects for Geldart A particles is used to simulate the behaviors typical of fast fluidization, including dynamic evolution of clusters as well as time- averaged axial and lateral voidage profiles. Diverse images of clusters are captured and the time-averaged profiles of voidage are shown to be in quantitative agreement with the present empirical correlation. The results based on different constitutive correlations of drag force s...
Riser reactors are frequently applied in catalytic processes involving rapid catalyst deactivation. ...
Steady state modeling based on time-averaged transport equations is a computationally efficient meth...
In this work, a new drag model for TFM simulation in gas solid bubbling fluidized beds was proposed,...
Drag force is a key parameter in the numerical modeling of gas-particle flow in circulating fluidize...
In this paper, an Eulerian–Lagrangian approach, in which the gas flow is solved by the volume-averag...
In the present paper, the possibilities to cover all fluidization states by a single drag law in ste...
In the present work, a qualitative analysis of the time-averaged gas–solid drag force in gas–solid f...
Fast fluidization of fine particles leads to formation of particle clusters, which significantly aff...
This dissertation focused on development and utilization of numerical and experimental approaches to...
Formation of particle clusters in fast fluidization of fine particles significantly affects the gas-...
Formation of particle clusters in fast fluidization of fine particles significantly affects the gas-...
This work presented a new scheme to establish structural parameters model, and the model was used to...
Formation of particle clusters in fast fluidization of fine particles significantly affects the gas-...
Drag correlations for fluid-particles interactions of multi-sized particle systems are important in ...
Fast fluidization of fine particles leads to formation of particle clusters, which significantly aff...
Riser reactors are frequently applied in catalytic processes involving rapid catalyst deactivation. ...
Steady state modeling based on time-averaged transport equations is a computationally efficient meth...
In this work, a new drag model for TFM simulation in gas solid bubbling fluidized beds was proposed,...
Drag force is a key parameter in the numerical modeling of gas-particle flow in circulating fluidize...
In this paper, an Eulerian–Lagrangian approach, in which the gas flow is solved by the volume-averag...
In the present paper, the possibilities to cover all fluidization states by a single drag law in ste...
In the present work, a qualitative analysis of the time-averaged gas–solid drag force in gas–solid f...
Fast fluidization of fine particles leads to formation of particle clusters, which significantly aff...
This dissertation focused on development and utilization of numerical and experimental approaches to...
Formation of particle clusters in fast fluidization of fine particles significantly affects the gas-...
Formation of particle clusters in fast fluidization of fine particles significantly affects the gas-...
This work presented a new scheme to establish structural parameters model, and the model was used to...
Formation of particle clusters in fast fluidization of fine particles significantly affects the gas-...
Drag correlations for fluid-particles interactions of multi-sized particle systems are important in ...
Fast fluidization of fine particles leads to formation of particle clusters, which significantly aff...
Riser reactors are frequently applied in catalytic processes involving rapid catalyst deactivation. ...
Steady state modeling based on time-averaged transport equations is a computationally efficient meth...
In this work, a new drag model for TFM simulation in gas solid bubbling fluidized beds was proposed,...