Traditional methods based on local equilibrium assumption are unsuitable to describe the non-linear and non-equilibrium mass transfer in turbulent fluidized beds (TFBs), especially for industrial-scale reactors. In this work, the structure-based mass balance equations are proposed to describe the transfer and reac-tion of component on the surface of particles. These equations are valid and reasonable whether mass transfer and chemical reaction are in local equilibrium or not. Since local equilibrium assumption is not used, the proposed method can directly describe the transfer-reaction systems in TFBs, which are not in local equilibrium. Moreover, the proposed mass balance equations have also considered the meso-scale flow of particles. Thi...
The Computational Fluid Dynamics - Discrete Element Method (CFD-DEM) method is extended by coupling ...
Modeling catalytic fixed bed reactors with a small tube-to-particle diameter ratio requires a detail...
AbstractThis article presents a CFD model to describe the interfacial reactive mass transfer that ta...
Traditional methods based on local equilibrium assumption are unsuitable to describe the non-linear ...
A structure-based mass-transfer model for turbulent fluidized beds (TFBs) was established according ...
A fluidized bed reactor embraces complex coupling among flow, heat/mass transfer and reaction kine...
The main objective of this work is to analyze the importance of the gas-solid interface transfer of ...
This paper analyzes the relationship between flow structure and mass transfer in fast fluidized beds...
The gas-solid mass transfer in the downer fluidized bed is analyzed theoretically in this work. Comp...
The effect of turbulence on the mass transfer between a fluid and embedded small heavy inertial part...
Fundamental research on fluidization should focus on the meso-scale structure of fluidized beds, to ...
In this work the limitations of the standard approaches to describe mass transfer in fluid-fluid sys...
Non-catalytic fluidized bed reactors (FBRs) have been utilized in various industries. In this study,...
We study mass transfer towards a solid spherical catalyst particle experiencing a first order irreve...
A level-set model is presented for simulating mass transfer or heat transfer in two-phase flows. The...
The Computational Fluid Dynamics - Discrete Element Method (CFD-DEM) method is extended by coupling ...
Modeling catalytic fixed bed reactors with a small tube-to-particle diameter ratio requires a detail...
AbstractThis article presents a CFD model to describe the interfacial reactive mass transfer that ta...
Traditional methods based on local equilibrium assumption are unsuitable to describe the non-linear ...
A structure-based mass-transfer model for turbulent fluidized beds (TFBs) was established according ...
A fluidized bed reactor embraces complex coupling among flow, heat/mass transfer and reaction kine...
The main objective of this work is to analyze the importance of the gas-solid interface transfer of ...
This paper analyzes the relationship between flow structure and mass transfer in fast fluidized beds...
The gas-solid mass transfer in the downer fluidized bed is analyzed theoretically in this work. Comp...
The effect of turbulence on the mass transfer between a fluid and embedded small heavy inertial part...
Fundamental research on fluidization should focus on the meso-scale structure of fluidized beds, to ...
In this work the limitations of the standard approaches to describe mass transfer in fluid-fluid sys...
Non-catalytic fluidized bed reactors (FBRs) have been utilized in various industries. In this study,...
We study mass transfer towards a solid spherical catalyst particle experiencing a first order irreve...
A level-set model is presented for simulating mass transfer or heat transfer in two-phase flows. The...
The Computational Fluid Dynamics - Discrete Element Method (CFD-DEM) method is extended by coupling ...
Modeling catalytic fixed bed reactors with a small tube-to-particle diameter ratio requires a detail...
AbstractThis article presents a CFD model to describe the interfacial reactive mass transfer that ta...