2017
DOI: 10.1002/aic.15883
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CFD as an approach to understand flammable dust 20 L standard test: Effect of the ignition time on the fluid flow

Abstract: in Wiley Online Library (wileyonlinelibrary.com)A computational study based on the Euler-Lagrange approach was developed for the characterization of flammable dusts in the 20 L sphere standard test. The aim of the study was to analyze some parameters that might affect the experimental data (e.g., cold turbulence and particle size). The turbulence of a wheat starch cloud was described with the Detached Eddy Simulation model. Both the pressure of the system and the RMS velocity were compared with the flow patter… Show more

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Cited by 14 publications
(10 citation statements)
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“…Moreover, the particle characteristics are more rapidly stable with a symmetrical nozzle and this stability is improved by using dust lifting instead of injection through a reservoir. It should also be underlined that no re-agglomeration phenomenon is visible during the dispersion, neither for aluminum nor for carbon black, which is not the case with powders such as starch (Vizcaya et al, 2018). Figure 4 shows the impact of the injection procedure on the particle size distribution of Corax N550.…”
Section: In Situ Particle Size Distribution Measurementsmentioning
confidence: 99%
See 1 more Smart Citation
“…Moreover, the particle characteristics are more rapidly stable with a symmetrical nozzle and this stability is improved by using dust lifting instead of injection through a reservoir. It should also be underlined that no re-agglomeration phenomenon is visible during the dispersion, neither for aluminum nor for carbon black, which is not the case with powders such as starch (Vizcaya et al, 2018). Figure 4 shows the impact of the injection procedure on the particle size distribution of Corax N550.…”
Section: In Situ Particle Size Distribution Measurementsmentioning
confidence: 99%
“…The PIV set-up which was used to determine the turbulence level of the dust clouds in the 20L sphere is described by Vizcaya et al (2018). The dispersion of dust particles may generate changes in the turbulence of the fluid depending on the diameter of the dust.…”
Section: Particle Image Velocimetry (Piv) -Turbulencementioning
confidence: 99%
“…Studies have investigated the explosion characteristics of dust alone or dust mixed with flammable gas 8–13 . The addition of hydrogen to fuels (i.e., the hydrogen‐enrichment) strongly induces non‐linear (i.e., synergistic) effects in terms of burning velocity, 14 interaction of the propagating flame with the turbulent flow field 15–16 ; thus, explosion behavior 17–18 .…”
Section: Introductionmentioning
confidence: 99%
“…It has been shown that particle‐size distribution, agglomerate strength, and concentration of dust particles affect their dispersion process within a confined environment, thus impacting on the likelihood and severity of explosion . Vizcaya et al reported that the mean diameter of particles decreased by 69% during dispersion . Yu et al discovered that the agglomeration of particles is related to the behavior of flame propagation in dust explosion .…”
Section: Introductionmentioning
confidence: 99%
“…[20][21][22][23][24] Vizcaya et al reported that the mean diameter of particles decreased by 69% during dispersion. 25 Yu et al discovered that the agglomeration of particles is related to the behavior of flame propagation in dust explosion. 26 Peter et al reported that smaller particles exhibited higher maximum rates of pressure rise [(dP/dt) max ] until a threshold diameter (below which either the explosivity plateaus [organic dust typically]).…”
mentioning
confidence: 99%