A multiphase model for fluid-particle flows with added mass and phase change

被引:0
|
作者
Boniou, Victor [1 ]
Fox, Rodney O. [1 ,2 ]
Posey, Jacob W.
Houim, Ryan W.
机构
[1] Iowa State Univ, Dept Chem & Biol Engn, Ames, IA 50011 USA
[2] Iowa State Univ, Ctr Multiphase Flow Res & Educ CoMFRE, Ames, IA USA
关键词
Gas-particle flow; Added-mass model; Dispersed multiphase flow; Mass and heat transfer; 2-FLUID MODEL; IMPLEMENTATION; COMBUSTION; SEQUEL; AUSM;
D O I
10.1016/j.cej.2024.157967
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
In our prior work, a kinetic-based model for fluid-particle flows with added mass was derived (Fox et al., 2020) and successfully validated for non-reacting cases without mass transfer (Boniou and Fox, 2023). In this work, the multiphase model is extended to allow for the added-mass phase to have a different temperature and density than the particle and bulk-fluid phases, and to account for mass transfer from the particle phase to the added-mass phase. For this purpose, mass and energy transfer between particles and their added mass, and the added-mass and bulk-fluid phases are included. As before, the particle-phase density rho(p) is assumed constant, but now the added-mass density rho(a) is allowed to differ from the bulk-fluid density rho(f). These densities are coupled through the assumption that their pressures are equal, i.e., p(a) = p(f), and determined by a fluid-phase equation of state. Since mass transfer will change the particle volume, an additional balance equation for the particle number density N-d is required to complete the multiphase model. The computational algorithm for the extended model is tested using sublimation and condensation of carbon-dioxide particles interacting with a strong shock wave.
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收藏
页数:14
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