2006
DOI: 10.1016/j.jlp.2005.06.005
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Simulation of dust explosions in complex geometries with experimental input from standardized tests

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Cited by 41 publications
(20 citation statements)
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References 16 publications
(15 reference statements)
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“…Skjold, Arntzen, Hansen, Storvik, and Eckhoff (2006) and presented results obtained with DESC 1.0b2, indicating a reasonably good agreement with experimental data obtained in relatively simple geometries such as silos (Eckhoff, Fuhre, & Pedersen, 1987;Hauert, Vogl, & Radandt, 1996) and interconnected vessel systems (Lunn, Holbrow, Andrews, & Gummer, 1996). Skjold, Pu et al (2005) simulated flame acceleration experiments with gas (methane) or dust (maize starch) reported by Pu (1988) and .…”
Section: Validation Of the Cfd Codesupporting
confidence: 70%
“…Skjold, Arntzen, Hansen, Storvik, and Eckhoff (2006) and presented results obtained with DESC 1.0b2, indicating a reasonably good agreement with experimental data obtained in relatively simple geometries such as silos (Eckhoff, Fuhre, & Pedersen, 1987;Hauert, Vogl, & Radandt, 1996) and interconnected vessel systems (Lunn, Holbrow, Andrews, & Gummer, 1996). Skjold, Pu et al (2005) simulated flame acceleration experiments with gas (methane) or dust (maize starch) reported by Pu (1988) and .…”
Section: Validation Of the Cfd Codesupporting
confidence: 70%
“…Algunos trabajos basados en estas técnicas ya han sido presentados (16,(26)(27)(28)(29) y abren un nuevo camino para mejorar la seguridad frente a explosiones. Sin embargo, la confianza en cualquier modelo numérico debe basarse en la validación de los resultados obtenidos mediante ensayos experimentales de explosión.…”
Section: Consideraciones Sobre La Protección De Silos Frente a Explosunclassified
“…It is not straightforward to unambiguously define an average velocity in a transient flow field, and hence to obtain well-defined values for the root-mean-square of the turbulent velocity fluctuations (Dahoe, Cant et al, 2001;Dahoe, van der Nat et al, 2001;Skjold, 2003), and certain assumptions must be invoked in order to extract decay laws for the turbulent integral length scale from such measurements (Dahoe, van (Pu et al, 1990); (b) in two cylindrical vessels, 7 and 22 l (Yan & Pu, 1999). performed with a very limited amount of dust in the system, and the influence of the presence of dust particles on the flow is usually unknown (Dahoe, van der Nat et al, 2001;Skjold, 2003). Finally, by using the level of turbulence at time of ignition as a reference, any decay of turbulence during the period from t ig to t* is neglected; an alternative approach involves using the level of turbulence at the inflection point as reference, hence neglecting any turbulence induced by combustion during the same period (Skjold, 2006;Skjold et al, 2005Skjold et al, , 2006.…”
Section: The Transient Nature Of Dispersion-induced Turbulencementioning
confidence: 99%
“…The concept of maximum effective burning velocity was suggested by Pu et al (1990), and a similar approach has recently been adopted for analyzing results from 20-l explosion vessels as input to the CFD-code DESC (Skjold, 2006;Skjold, Arntzen, Hansen, Storvik, & Eckhoff, 2006;Skjold et al, 2005). The main purpose of the present study is to investigate practical procedures for determining u eff,max from measured pressure-time histories in closed combustion vessels, and to compare results obtained in different explosion vessels.…”
Section: Introductionmentioning
confidence: 99%