The gas-solid mass transfer in the downer fluidized bed is analyzed theoretically in this work. Compared to the homogeneous assumption in each calculating grid, a structure-based model was proposed that the process was divided into the mass transfer in the cluster and dispersed phases. Simulations were performed with the cooperation of the Euler-Euler two-fluid method. The model predictions are in good agreement with the previous reported experimental measurements under a wide range of operating conditions. Simulated ozone profiles show a sharp conversion in the acceleration region, and a gentle conversion in the fully developed region. The transition point is well consistent with the boundary measured experimentally. These results show tha...
Catalytic oxidation of carbon monoxide over a Pt catalyst was employed as a model reaction to invest...
This work presents a new structure-based drag model for downer reactors combining with the computati...
Catalytic ozone decomposition was conducted in an 8.20 m high, 0.09 m inner diameter downer. The ozo...
The gas-solid mass transfer in the downer fluidized bed is analyzed theoretically in this work. Comp...
This paper analyzes the relationship between flow structure and mass transfer in fast fluidized beds...
A structure-based mass-transfer model for turbulent fluidized beds (TFBs) was established according ...
The effects of meso-structure on gas-solid mass transfer in bubbling fluidized beds (BFBs) were stud...
This article is to test the EMMS-based multiscale mass transfer model through computational fluid dy...
To improve the accuracy of simulating the heterogeneous flow in a circulating fluidized bed (CFB) do...
In this paper, a multiphase model applied to a downer reactor is proposed, where the gas-solid model...
The fluid dynamics of a downer reactor were numerically resolved by adapting a mathematical conserva...
International audienceRadial distribution profiles of ozone concentrations were measured along an 8....
Catalytic decomposition of ozone was carried out in a 15-m high, 90-mm inner diameter downer reactor...
In the coalescence zone, we obtained ozone concentration profiles of pairs of bubbles in vertical an...
Traditional methods based on local equilibrium assumption are unsuitable to describe the non-linear ...
Catalytic oxidation of carbon monoxide over a Pt catalyst was employed as a model reaction to invest...
This work presents a new structure-based drag model for downer reactors combining with the computati...
Catalytic ozone decomposition was conducted in an 8.20 m high, 0.09 m inner diameter downer. The ozo...
The gas-solid mass transfer in the downer fluidized bed is analyzed theoretically in this work. Comp...
This paper analyzes the relationship between flow structure and mass transfer in fast fluidized beds...
A structure-based mass-transfer model for turbulent fluidized beds (TFBs) was established according ...
The effects of meso-structure on gas-solid mass transfer in bubbling fluidized beds (BFBs) were stud...
This article is to test the EMMS-based multiscale mass transfer model through computational fluid dy...
To improve the accuracy of simulating the heterogeneous flow in a circulating fluidized bed (CFB) do...
In this paper, a multiphase model applied to a downer reactor is proposed, where the gas-solid model...
The fluid dynamics of a downer reactor were numerically resolved by adapting a mathematical conserva...
International audienceRadial distribution profiles of ozone concentrations were measured along an 8....
Catalytic decomposition of ozone was carried out in a 15-m high, 90-mm inner diameter downer reactor...
In the coalescence zone, we obtained ozone concentration profiles of pairs of bubbles in vertical an...
Traditional methods based on local equilibrium assumption are unsuitable to describe the non-linear ...
Catalytic oxidation of carbon monoxide over a Pt catalyst was employed as a model reaction to invest...
This work presents a new structure-based drag model for downer reactors combining with the computati...
Catalytic ozone decomposition was conducted in an 8.20 m high, 0.09 m inner diameter downer. The ozo...