Coupling CFD-DEM and microkinetic modeling of surface chemistry for the simulation of catalytic fluidized systems

被引:20
|
作者
Uglietti, Riccardo [1 ]
Bracconi, Mauro [1 ]
Maestri, Matteo [1 ]
机构
[1] Politecn Milan, Lab Catalysis & Catalyt Proc, Dipartimento Energia, Via La Masa 34, I-20156 Milan, Italy
来源
REACTION CHEMISTRY & ENGINEERING | 2018年 / 3卷 / 04期
基金
欧洲研究理事会;
关键词
DISCRETE PARTICLE SIMULATION; SITU ADAPTIVE TABULATION; CH4 PARTIAL OXIDATION; GAS-SOLID FLOW; NUMERICAL-SIMULATION; HEAT-TRANSFER; BED; COMBUSTION; REACTORS; VALIDATION;
D O I
10.1039/c8re00050f
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
In this work, we propose numerical methodologies to combine detailed microkinetic modeling and Eulerian-Lagrangian methods for the multiscale simulation of fluidized bed reactors. In particular, we couple the hydrodynamics description by computational fluid dynamics and the discrete element method (CFD-DEM) with the detailed surface chemistry by means of microkinetic modeling. The governing equations for the gas phase are solved through a segregated approach. The mass and energy balances for each catalytic particle, instead, are integrated adopting both the coupled and the operator-splitting approaches. To reduce the computational burden associated with the microkinetic description of the surface chemistry, in situ adaptive tabulation (ISAT) is employed together with operator-splitting. The catalytic partial oxidation of methane and steam reforming on Rh are presented as a showcase to assess the capability of the methods. An accurate description of the gas and site species is achieved along with up to 4 times speed-up of the simulation, thanks to the combined effect of operator-splitting and ISAT. The proposed approach represents an important step for the first-principles based multiscale analysis of fluidized reactive systems.
引用
收藏
页码:527 / 539
页数:13
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