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Haosheng Zhou - One of the best experts on this subject based on the ideXlab platform.

  • dem les simulation of coal combustion in a bubbling fluidized bed part ii coal combustion at the Particle level
    Chemical Engineering Science, 2004
    Co-Authors: Haosheng Zhou, Gilles Flama, Daniel J Gauthie
    Abstract:

    The discrete element method-large eddy simulation (DEM-LES) is used to model coal combustion at the Particle level in a bubbling fluidized bed. The gas phase is modelled as a continuum and the solid phase is modeled by DEM. Chemical reactions consist in the heterogeneous reactions of char with O2, CO, CO2, NO, and N2O, and in the homogeneous reactions involving CO, O2, NO, and N2O. The Colliding ParticleParticle heat transfer is based on the analysis of the elastic deformation of the spheres during their contact. The model predicts the effects of the Particle heterogeneous flow structure on the thermal characteristics of coal Particles when heating and burning, and the gaseous emissions from a fluidized sand–coal binary mixture. The heating rates are 1627 and for, respectively, 0.8 and diameter coal Particles fed into the fluidized bed. The instantaneous contribution of the collision heat transfer is weak, less than 5.0% of the total power exchanges (coal combustion, radiation, convection and collision) during the heating and 1.5% during the combustion. The temperature of the coal Particles exceeds the bed temperature, which is in qualitative agreement with experimental data from literature. The effects of the diameter of coal Particles, of the bed temperature, and of the inlet gas velocity on the thermal characteristics are also studied.

  • dem les simulation of coal combustion in a bubbling fluidized bed part ii coal combustion at the Particle level
    Chemical Engineering Science, 2004
    Co-Authors: Haosheng Zhou, Gilles Flamant, Daniel J Gauthier
    Abstract:

    The discrete element method-large eddy simulation (DEM-LES) is used to model coal combustion at the Particle level in a bubbling fluidized bed. The gas phase is modelled as a continuum and the solid phase is modeled by DEM. Chemical reactions consist in the heterogeneous reactions of char with O2, CO, CO2, NO, and N2O, and in the homogeneous reactions involving CO, O2, NO, and N2O. The Colliding ParticleParticle heat transfer is based on the analysis of the elastic deformation of the spheres during their contact. The model predicts the effects of the Particle heterogeneous flow structure on the thermal characteristics of coal Particles when heating and burning, and the gaseous emissions from a fluidized sand–coal binary mixture. The heating rates are 1627 and for, respectively, 0.8 and diameter coal Particles fed into the fluidized bed. The instantaneous contribution of the collision heat transfer is weak, less than 5.0% of the total power exchanges (coal combustion, radiation, convection and collision) during the heating and 1.5% during the combustion. The temperature of the coal Particles exceeds the bed temperature, which is in qualitative agreement with experimental data from literature. The effects of the diameter of coal Particles, of the bed temperature, and of the inlet gas velocity on the thermal characteristics are also studied.

Hoanglong Ngo - One of the best experts on this subject based on the ideXlab platform.

Jacek Malecki - One of the best experts on this subject based on the ideXlab platform.

  • strong solutions of non Colliding Particle systems
    arXiv: Probability, 2014
    Co-Authors: Piotr Graczyk, Jacek Malecki
    Abstract:

    We study systems of stochastic differential equations describing positions x_1,x_2,...,x_p of p ordered Particles, with inter-Particles repulsions of the form H_{ij}(x_i,x_j)/(x_i-x_j). We show the existence of strong and pathwise unique non-Colliding solutions of the system with a Colliding initial point x_1(0)\leq ...\leq x_p(0) in the whole generality, under natural assumptions on the coefficients of the equations.

  • strong solutions of non Colliding Particle systems
    Electronic Journal of Probability, 2014
    Co-Authors: Piotr Graczyk, Jacek Malecki
    Abstract:

    We study systems of stochastic differential equations describing positions $x_1,x_2,\ldots,x_p$ of $p$ ordered Particles, with inter-Particles repulsions of the form $\displaystyle{\frac{H_{ij}(x_i,x_j)}{x_i-x_j}}$. We show the existence of strong and pathwise unique non-Colliding solutions of the system with a Colliding initial point $x_1(0)\leq \ldots\leq x_p(0)$ in the whole generality, under natural assumptions on the coefficients of the equations.

Daniel J Gauthie - One of the best experts on this subject based on the ideXlab platform.

  • dem les simulation of coal combustion in a bubbling fluidized bed part ii coal combustion at the Particle level
    Chemical Engineering Science, 2004
    Co-Authors: Haosheng Zhou, Gilles Flama, Daniel J Gauthie
    Abstract:

    The discrete element method-large eddy simulation (DEM-LES) is used to model coal combustion at the Particle level in a bubbling fluidized bed. The gas phase is modelled as a continuum and the solid phase is modeled by DEM. Chemical reactions consist in the heterogeneous reactions of char with O2, CO, CO2, NO, and N2O, and in the homogeneous reactions involving CO, O2, NO, and N2O. The Colliding ParticleParticle heat transfer is based on the analysis of the elastic deformation of the spheres during their contact. The model predicts the effects of the Particle heterogeneous flow structure on the thermal characteristics of coal Particles when heating and burning, and the gaseous emissions from a fluidized sand–coal binary mixture. The heating rates are 1627 and for, respectively, 0.8 and diameter coal Particles fed into the fluidized bed. The instantaneous contribution of the collision heat transfer is weak, less than 5.0% of the total power exchanges (coal combustion, radiation, convection and collision) during the heating and 1.5% during the combustion. The temperature of the coal Particles exceeds the bed temperature, which is in qualitative agreement with experimental data from literature. The effects of the diameter of coal Particles, of the bed temperature, and of the inlet gas velocity on the thermal characteristics are also studied.

Daniel J Gauthier - One of the best experts on this subject based on the ideXlab platform.

  • dem les simulation of coal combustion in a bubbling fluidized bed part ii coal combustion at the Particle level
    Chemical Engineering Science, 2004
    Co-Authors: Haosheng Zhou, Gilles Flamant, Daniel J Gauthier
    Abstract:

    The discrete element method-large eddy simulation (DEM-LES) is used to model coal combustion at the Particle level in a bubbling fluidized bed. The gas phase is modelled as a continuum and the solid phase is modeled by DEM. Chemical reactions consist in the heterogeneous reactions of char with O2, CO, CO2, NO, and N2O, and in the homogeneous reactions involving CO, O2, NO, and N2O. The Colliding ParticleParticle heat transfer is based on the analysis of the elastic deformation of the spheres during their contact. The model predicts the effects of the Particle heterogeneous flow structure on the thermal characteristics of coal Particles when heating and burning, and the gaseous emissions from a fluidized sand–coal binary mixture. The heating rates are 1627 and for, respectively, 0.8 and diameter coal Particles fed into the fluidized bed. The instantaneous contribution of the collision heat transfer is weak, less than 5.0% of the total power exchanges (coal combustion, radiation, convection and collision) during the heating and 1.5% during the combustion. The temperature of the coal Particles exceeds the bed temperature, which is in qualitative agreement with experimental data from literature. The effects of the diameter of coal Particles, of the bed temperature, and of the inlet gas velocity on the thermal characteristics are also studied.