2009
DOI: 10.1016/j.ces.2009.04.042
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Practical scaling considerations for dense gas fluidized beds interacting with the air-supply system

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Cited by 4 publications
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“…Due to the complex flow behavior that characterizes gas-solid systems, a complete description of circulating fluidized bed hydrodynamics remains a challenging task (Detamore et al, 2001). In the absence of alternative methods, scaling rules developed over the last two decades proved to be a reasonable tool for the scale-up and scale-down of fluidization processes (Sierra et al, 2009). As has been noted by Horio (1996), there have been three different approaches to the scaling law of fluidized beds: classical dimensional analysis (e.g., Buckingham π-theorem), differential equations (or, more specifically, non-dimensionalization of the continuum equations that describe multiphase flows) and theoretical solutions and experimental correlations.…”
Section: Introductionmentioning
confidence: 99%
“…Due to the complex flow behavior that characterizes gas-solid systems, a complete description of circulating fluidized bed hydrodynamics remains a challenging task (Detamore et al, 2001). In the absence of alternative methods, scaling rules developed over the last two decades proved to be a reasonable tool for the scale-up and scale-down of fluidization processes (Sierra et al, 2009). As has been noted by Horio (1996), there have been three different approaches to the scaling law of fluidized beds: classical dimensional analysis (e.g., Buckingham π-theorem), differential equations (or, more specifically, non-dimensionalization of the continuum equations that describe multiphase flows) and theoretical solutions and experimental correlations.…”
Section: Introductionmentioning
confidence: 99%