Numerical investigation of the grid spatial resolution and the anisotropic character of EMMS in CFB multiphase flow

During the last years, considerable efforts have been made for the optimization of numerical methods simulating the operation of the Circulating Fluidized Bed Combustors (CFBC), which imply both the accuracy increase and the computational cost decrease. A foremost goal is the efficient description of its operation under isothermal conditions and the in-depth understanding of the governing complex multiphase flow mechanisms. Grid construction and the calculation of the drag force experienced by the inert material in the two-phase flow are two important parameters for the optimization of the numerical approaches in the case of CFB simulation. The aim of the present investigation is to investigate both the effect of grid density distribution on simulation results and the validity of an anisotropic approach for the drag force calculation through an Energy Minimization Multi-Scale (EMMS) scheme. Grid density distribution is found to affect the numerical accuracy and the real time of simulations. Uniform grid density distribution is found to be the most efficient choice in terms of balance between computational cost and numerical accuracy. On the other hand, EMMS scheme improves the efficiency of detecting complex particle structures (clusters) without an explicit modeling of these spatio-temporal formations. Moreover, applying EMMS scheme only for calculation of the z-component of drag force yielded better numerical results compared to a constant interphase momentum exchange coefficient for all the three directions.

[1]  Jinghai Li,et al.  Virtual experimentation through 3D full-loop simulation of a circulating fluidized bed , 2008 .

[2]  Tron Solberg,et al.  A three-dimensional simulation of gas/particle flow and ozone decomposition in the riser of a circulating fluidized bed , 2004 .

[3]  Kelvin Chu,et al.  Numerical simulation of complex particle-fluid flows , 2006 .

[4]  Dimitri Gidaspow,et al.  Computation of flow patterns in circulating fluidized beds , 1990 .

[5]  G. Itskos,et al.  Heavy metal characterization of CFB-derived coal fly ash , 2011 .

[6]  Joel H. Ferziger,et al.  Computational methods for fluid dynamics , 1996 .

[7]  R. Jackson,et al.  Frictional–collisional constitutive relations for granular materials, with application to plane shearing , 1987, Journal of Fluid Mechanics.

[8]  Panagiotis Grammelis,et al.  An advanced EMMS scheme for the prediction of drag coefficient under a 1.2 MWth CFBC isothermal flow—Part II: Numerical implementation , 2010 .

[9]  Lounes Tadrist,et al.  Computational study of fluctuating motions and cluster structures in gas–particle flows , 2002 .

[10]  Guodong Liu,et al.  Fluid dynamic simulation in a chemical looping combustion with two interconnected fluidized beds , 2011 .

[11]  Wei Ge,et al.  Focusing on the meso-scales of multi-scale phenomena-In search for a new paradigm in chemical engineering , 2010 .

[12]  Huilin Lu,et al.  Numerical study on the cluster flow behavior in the riser of circulating fluidized beds , 2009 .

[13]  Tron Solberg,et al.  Comparison of multifluid and discrete particle modelling in numerical predictions of gas particle flow in circulating fluidised beds , 2004 .

[14]  Hugo A. Jakobsen,et al.  A Sensitivity Study of the Two-Fluid Model Closure Parameters (β, e) Determining the Main Gas−Solid Flow Pattern Characteristics , 2010 .

[15]  Jan Vierendeels,et al.  An extension of the preconditioned advection upstream splitting method for 3D two-phase flow calculations in circulating fluidized beds , 2002 .

[16]  Wei Ge,et al.  CFD simulation of concurrent-up gas-solid flow in circulating fluidized beds with structure-dependent drag coefficient , 2003 .

[17]  H. Arastoopour,et al.  Simulation of particles and gas flow behavior in the riser section of a circulating fluidized bed using the kinetic theory approach for the particulate phase , 2000 .

[18]  J. G. Yates,et al.  Fluidization engineering: Second edition , 1993 .

[19]  Panagiotis Grammelis,et al.  Optimization of Computational Performance and Accuracy in 3-D Transient CFD Model for CFB Hydrodynamics Predictions , 2007 .

[20]  Hydrodynamics of a Cluster Descending at the Wall of a CFB Riser - Numerical Study , 2011 .

[21]  Wei Wang,et al.  Searching for a mesh-independent sub-grid model for CFD simulation of gas–solid riser flows , 2009 .

[22]  Hamid Arastoopour,et al.  Hydrodynamic analysis of dilute gas—solids flow in a vertical pipe , 1990 .

[23]  Lin Ma,et al.  Modelling methods for co-fired pulverised fuel furnaces , 2009 .

[24]  X. Pengfei,et al.  Simulation of particles and gas flow behavior in a riser using a filtered two-fluid model , 2011 .

[25]  Wei Ge,et al.  Eulerian simulation of heterogeneous gas–solid flows in CFB risers: EMMS-based sub-grid scale model with a revised cluster description , 2008 .

[26]  Wu Yu-xin Conceptual Design of an 800MWe Supercritical Pressure Circulating Fluidized Bed Boiler , 2004 .

[27]  D. Zhang,et al.  High-resolution three-dimensional numerical simulation of a circulating fluidized bed , 2001 .

[28]  C. Wen Mechanics of Fluidization , 1966 .

[29]  Joachim Werther,et al.  CFD-simulation of a circulating fluidized bed riser , 2009 .

[30]  Fariborz Taghipour,et al.  Computational fluid dynamics of a circulating fluidized bed under various fluidization conditions , 2008 .

[31]  G. Itskos,et al.  Synthesis of CFB-Coal Fly Ash Clay Bricks and Their Characterisation , 2011 .

[32]  Kai H. Luo,et al.  Two-dimensional and three-dimensional computational studies of hydrodynamics in the transition from bubbling to circulating fluidised bed , 2010 .

[33]  Craig Hawthorne,et al.  Hydrodynamic analysis of a 10 kWth Calcium Looping Dual Fluidized Bed for post-combustion CO2 capture , 2010 .

[34]  Nikolaos Koukouzas,et al.  Removal of heavy metals from wastewater using CFB-coal fly ash zeolitic materials. , 2010, Journal of hazardous materials.

[35]  Rajamani Krishna,et al.  Comparative analysis of CFD models of dense gas–solid systems , 2001 .

[36]  Jesse Zhu,et al.  Characterization of fluidization behavior in the bottom region of CFB risers , 2008 .

[37]  Fei Wei,et al.  The solid flow structure in a circulating fluidized bed riser/downer of 0.42-m diameter , 2003 .

[38]  L. Huilin,et al.  Numerical predictions of flow behavior and cluster size of particles in riser with particle rotation model and cluster-based approach , 2008 .

[39]  Wei Wang,et al.  Simulation of gas-solid two-phase flow by a multi-scale CFD approach - Extension of the EMMS model to the sub-grid level , 2007 .