2014
DOI: 10.1016/j.powtec.2014.04.095
|View full text |Cite
|
Sign up to set email alerts
|

Challenges of DEM: I. Competing bottlenecks in parallelization of gas–solid flows

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
3
1
1

Citation Types

0
11
0

Year Published

2015
2015
2022
2022

Publication Types

Select...
7
1

Relationship

3
5

Authors

Journals

citations
Cited by 25 publications
(11 citation statements)
references
References 25 publications
0
11
0
Order By: Relevance
“…The situation worsens for smaller particles, since the time step is 4 proportional to particle size. For example, our recent study on fine particles (Liu and Hrenya, 2014) showed that even for a pseudo-2D fluidized bed (bed with thickness of 1 particle diameter), the bed width attainable by DEM-CFD is limited to ~ 1 cm, much smaller than typical experiments with bed width and thickness > 10 cm. To overcome this computational challenge, it is desirable to increase the simulation time step or have a scale-independent parameter to compare with experiments.…”
Section: Introductionmentioning
confidence: 92%
“…The situation worsens for smaller particles, since the time step is 4 proportional to particle size. For example, our recent study on fine particles (Liu and Hrenya, 2014) showed that even for a pseudo-2D fluidized bed (bed with thickness of 1 particle diameter), the bed width attainable by DEM-CFD is limited to ~ 1 cm, much smaller than typical experiments with bed width and thickness > 10 cm. To overcome this computational challenge, it is desirable to increase the simulation time step or have a scale-independent parameter to compare with experiments.…”
Section: Introductionmentioning
confidence: 92%
“…In DEM, 1HZWRQ ¶V HTXDWLRQV RI PRWLRQ DUH VROYHG IRU every particle in the domain, and therefore adjusting the particle properties for each particle is straightforward [4]. However, tracking the positions of every particle in the domain requires a large computational overhead, and consequently the number of particles, or size of the system, that can be simulated with DEM is limited to orders of magnitude smaller than realistic processes [5]. In TFM, the particle phase and fluid (liquid or gas) phase are treated as interpenetrating, interacting continua, hence the particle phase is treated as a fluid (i.e., individual particles are not considered), and mass and momentum balances are solved for each phase.…”
Section: Introductionmentioning
confidence: 99%
“…Since its initial release, MFIX has been successfully employed to model a variety of multiphase flow problems relevant to industrial and energy-related applications [13,14,15,16,17,18,19,20,21]. Due to the inherent complexity and diverse range of spatial/temporal scales involved in multiphase flow simulations, several initiatives were carried out to reduce the time-to-solution through performance improvements [22,23,24,25,26,27,28,29,30].…”
Section: Department Of Energymentioning
confidence: 99%