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Coupling particle scale model and SuperDEM-CFD for multiscale simulation of biomass pyrolysis in a packed bed pyrolyzer
被引:47
|作者:
Gao, Xi
[1
,2
]
Yu, Jia
[1
]
Lu, Liqiang
[1
,2
]
Rogers, William A.
[1
]
机构:
[1] Natl Energy Technol Lab, Morgantown, WV 26506 USA
[2] Leidos Res Support Team, Morgantown, WV USA
关键词:
biomass;
CFD‐
DEM;
MFiX;
non‐
spherical;
pyrolysis;
superquadric;
HEAT-TRANSFER COEFFICIENTS;
DIRECT NUMERICAL-SIMULATION;
VERIFICATION;
CONDUCTION;
KINETICS;
MASS;
D O I:
10.1002/aic.17139
中图分类号:
TQ [化学工业];
学科分类号:
0817 ;
摘要:
An efficient biomass pyrolysis process requires a comprehensive understanding of the chemical and physical phenomena that occur at multi-length and time scales. In this study, a multiscale computational approach was developed and validated for biomass pyrolysis in a packed-bed reactor by integrating pyrolysis kinetics, a particle scale model, and Superquadric Discrete Element Method-Computational Fluid Dynamics (SuperDEM-CFD) in open-source code MFiX. A one-dimensional particle-scale model that discretizes the characteristic length of biomass particle into layers was developed to predict the intraparticle phenomena inside a single particle. The 1D model was validated by comparing it with a single biomass particle pyrolysis experiment. A recently developed SuperDEM-CFD model was employed to simulate the non-spherical particle-particle contact and fluid-particle interaction. The coupled model was applied to simulate the pyrolysis of cubic biomass particles in a packed bed and validated by comparing with experimental data. Simulation with and without particle-scale model was compared, and the effect of the gas-solid heat transfer models was also investigated.
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页数:15
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