Thermal DEM–CFD modeling and simulation of heat transfer through packed bed

Abstract Heat transfer between particles takes place in a variety of industrial applications, but because of the stress and contact heterogeneities inherent to these applications, it is poorly understood, even in simple cases. Although particle–particle heat transfer is relatively weak compared with particle–fluid convection heat transfer, it may become very important in applications such as packed beds, where the fluid flow can be neglected or where fluid/particle stagnation areas can be observed. During our previous studies, CFD–DEM models and numerical simulations were developed to account for momentum and heat transfer between the fluid and the solid particles. The predictions of the simulations were validated with experimental data. In the present study, particle–particle and particle–wall heat transfer models were developed and integrated into our in-house unsteady three-dimensional discrete element method (DEM) software. Heat transfer simulations for predicting the effective thermal conductivity (ETC) of particulate beds under compression were conducted to validate these models with published experimental data. The results showed good agreement with the experimental data, and it was found that heat conduction through the bed's pores cannot be neglected even when particle thermal conductivity is much larger than that of the air. The influence of particle roughness on heat transfer through packed bed was examined. It was found that heat conduction through the packed bed pores cannot be neglected for rough particles.

[1]  Fernando J. Muzzio,et al.  Experimentally validated computations of heat transfer in granular materials in rotary calciners , 2010 .

[2]  K. Malone,et al.  Particle-scale simulation of heat transfer in liquid-fluidised beds , 2008 .

[3]  M. Hunt,et al.  Discrete element simulations for granular material flows: effective thermal conductivity and self-diffusivity , 1997 .

[4]  J. Greenwood,et al.  Contact of nominally flat surfaces , 1966, Proceedings of the Royal Society of London. Series A. Mathematical and Physical Sciences.

[5]  A. Yu,et al.  A new computational method for studying heat transfer in fluid bed reactors , 2010 .

[6]  H. Kalman,et al.  A theoretical model for effective thermal conductivity (ETC) of particulate beds under compression , 2004 .

[7]  D. Mason,et al.  A computational investigation of transient heat transfer in pneumatic transport of granular particles , 2000 .

[8]  Haim Kalman,et al.  DEM simulation of particle attrition in dilute-phase pneumatic conveying , 2011 .

[9]  Runyu Yang,et al.  Discrete particle simulation of particulate systems: A review of major applications and findings , 2008 .

[10]  H. Kalman,et al.  The effect of compression and preconsolidation on the effective thermal conductivity of particulate beds , 2003 .

[11]  Aibing Yu,et al.  Finite element modeling of the transient heat conduction between colliding particles , 2008 .

[12]  Joseph J. McCarthy,et al.  Stress effects on the conductivity of particulate beds , 2002 .

[13]  Grant M. Campbell,et al.  Discrete Modeling and Suggested Measurement of Heat Transfer in Gas–Solids Flows , 2003 .

[14]  Tawatchai Charinpanitkul,et al.  Prediction of gas-particle dynamics and heat transfer in a two-dimensional spouted bed , 2005 .

[15]  P. Haff Grain flow as a fluid-mechanical phenomenon , 1983, Journal of Fluid Mechanics.

[16]  Arun S. Mujumdar,et al.  A Numerical Study of Heat Transfer Mechanisms in Gas–Solids Flows Through Pipes Using a Coupled CFD and DEM Model , 2003 .

[17]  Masayuki Horio,et al.  DEM simulation of fluidized beds for gas-phase olefin polymerization , 1999 .

[18]  Jérôme Fortin,et al.  Discrete modeling of granular flow with thermal transfer: Application to the discharge of silos , 2009 .

[19]  Jintang Li,et al.  APPLICATION OF THE DISCRETE ELEMENT MODELLING IN AIR DRYING OF PARTICULATE SOLIDS , 2002 .

[20]  Yongzhi Zhao,et al.  Particle‐scale simulation of the flow and heat transfer behaviors in fluidized bed with immersed tube , 2009 .

[21]  Avi Levy,et al.  Modeling of Heat Transfer in Pneumatic Conveyer Using a Combined DEM-CFD Numerical Code , 2010 .

[22]  Joseph J. McCarthy,et al.  Heat conduction in granular materials , 2001 .

[23]  Gerry E. Schneider,et al.  Thermal Contact Resistance of Nonconforming Rough Surfaces, Part 1: Contact Mechanics Model , 2003 .

[24]  Paul Zulli,et al.  Evaluation of effective thermal conductivity from the structure of a packed bed , 1999 .

[25]  Y. T. Feng,et al.  Discrete thermal element modelling of heat conduction in particle systems: Basic formulations , 2008, J. Comput. Phys..

[26]  Paul Zulli,et al.  Particle scale study of heat transfer in packed and bubbling fluidized beds , 2009 .

[27]  Joe D. Goddard,et al.  Simulation of the quasi-static mechanics and scalar transport properties of ideal granular assemblages , 1995 .