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Title: Assessment of different coarse graining strategies to simulate polydisperse gas-solids flow

Journal Article · · Chemical Engineering Science
ORCiD logo [1];  [1];  [2]; ORCiD logo [1]
  1. National Energy Technology Lab. (NETL), Morgantown, WV (United States)
  2. National Energy Technology Lab. (NETL), Morgantown, WV (United States); AECOM, Morgantown, WV (United States)

Continuum methods require the additional development of solids stress closures for polydisperse powders based on complex kinetic theories that are non-trivial to develop, code, and numerically converge for the wide range of fluidization regimes from very dilute to dense/frictional flow limit. On the other hand, it is straightforward to model the flow of polydisperse granular materials by treating particles as discrete rigid bodies that are tracked following simple physical laws of motion. The coarsening of these discrete methods by lumping several particles in a parcel alleviates the significant computational cost associated with these discrete methods while introducing some inaccuracies in the numerical results. In this research, we explore two different coarse graining methods that can be applied to polydisperse powders, namely the same statistic weight method (SSW) and the same size parcel method (SSP), and assess their accuracy by comparison with the finest simulation results obtained with a discrete element method (DEM). For Geldart group B powders fluidized at a relative low superficial velocity, the numerical results indicate that the SSW is more accurate than the SSP method. For type A powders fluidized at relatively high velocity, these two methods predict similar results. Interestingly, up to four times increase in the speed of simulation of the SSP method was obtained because the original polydisperse powder is scaled to a mono-disperse system in terms of particle-particle collision. Lastly, these results suggest that the SSP method is more favorable for the simulation of fluidized beds due to its accuracy and efficiency while the SSW method may be used for granular flow and dense fluidized bed systems where capturing the size segregation of particles due to collision is important.

Research Organization:
National Energy Technology Laboratory (NETL), Pittsburgh, PA, Morgantown, WV (United States)
Sponsoring Organization:
USDOE Office of Fossil Energy (FE)
OSTI ID:
1461078
Alternate ID(s):
OSTI ID: 1548801
Report Number(s):
NETL-PUB-21465; PII: S0009250918300034
Journal Information:
Chemical Engineering Science, Vol. 179, Issue C; ISSN 0009-2509
Publisher:
ElsevierCopyright Statement
Country of Publication:
United States
Language:
English
Citation Metrics:
Cited by: 35 works
Citation information provided by
Web of Science

References (27)

Fluid Mechanical Description of Fluidized Beds. Equations of Motion journal November 1967
Estimation of Numerical Errors Related to Some Basic Assumptions in Discrete Particle Methods journal November 2010
Challenges of DEM: II. Wide particle size distributions journal September 2014
On an efficient hybrid soft and hard sphere collision integration scheme for DEM journal October 2016
Three-dimensional CFD-PBM coupled model of the temperature fields in fluidized-bed polymerization reactors journal March 2011
Applicability of a coarse-grained CFD–DEM model on dense medium cyclone journal May 2016
Application of the direct quadrature method of moments to polydisperse gas–solid fluidized beds journal January 2004
Multiscale Discrete Supercomputing - A Game Changer for Process Simulation? journal March 2015
Digital image analysis measurements of bed expansion and segregation dynamics in dense gas-fluidised beds journal December 2003
Influence of particle size distribution on the performance of fluidized bed reactors journal October 1991
Numerical Investigation of the Ability of Salt Tracers to Represent the Residence Time Distribution of Fluidized Catalytic Cracking Particles journal November 2017
Influence of grid resolution, parcel size and drag models on bubbling fluidized bed simulation journal October 2017
An efficient and reliable predictive method for fluidized bed simulation journal June 2017
Extension of a coarse grained particle method to simulate heat transfer in fluidized beds journal August 2017
Computer virtual experiment on fluidized beds using a coarse-grained discrete particle method—EMMS-DPM journal November 2016
EMMS-based discrete particle method (EMMS–DPM) for simulation of gas–solid flows journal December 2014
Coarse-Grained-Particle Method for Simulation of Liquid–Solids Reacting Flows journal September 2016
Modeling and numerical simulation of particulate flows by the Eulerian–Lagrangian approach journal October 2001
Slow relaxation and compaction of granular systems journal February 2005
Why the Brazil nuts are on top: Size segregation of particulate matter by shaking journal March 1987
Verification and validation of a coarse grain model of the DEM in a bubbling fluidized bed journal May 2014
The effect of particle size distribution on the performance of a catalytic fluidized bed reactor journal January 1990
Discrete particle simulation of two-dimensional fluidized bed journal October 1993
Coarse-grained discrete particle simulations of particle segregation in rotating fluidized beds in vortex chambers journal August 2017
Numerical simulation of the gas-solid flow in a fluidized bed by combining discrete particle method with computational fluid dynamics journal August 1997
Quasi-real-time simulation of rotating drum using discrete element method with parallel GPU computing journal August 2011
Assessment of polydisperse drag models for the size segregation in a bubbling fluidized bed using discrete particle method journal March 2017

Cited By (3)

Dynamics of segregation and fluidization of binary mixtures in a cylindrical fluidized bed journal June 2019
Experimental methods in chemical engineering: Unresolved CFD‐DEM journal October 2019
Comprehensive experimental investigation on biomass‐glass beads binary fluidization: A data set for CFD model validation journal October 2019

Figures / Tables (15)


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