2019
DOI: 10.1016/j.mineng.2019.105926
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The distribution of bed density in an air dense medium fluidized bed with single and binary mixtures of Geldart B and/or D particles

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Cited by 11 publications
(8 citation statements)
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“…Otherwise, V sub is less than V . For the prediction of fluidized bed density ( ρ bed ), a general correlation has been proposed in earlier work and is shown as ρ b e d = ( 1 ε m f ) ( ρ p ρ g ) [ 1 Y / false( 1 + 1.3 ( H / 2 + 4 A D 0.5 ) false( U g U m f false) 0.8 false) ] where ε mf is the bed voidage at the minimum fluidization state, ρ g is the gas density, ρ p is the density of solid particles, H is the height of the fluidized bed, A D is the area of each orifice on the gas distributor, U g is the superficial gas velocity, U mf is the minimum fluidization velocity, and Y is the correction factor for the Two-phase Theory of Fluidization. For Geldart Group A powders, the Y value is very close to 0.85 .…”
Section: Theorymentioning
confidence: 99%
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“…Otherwise, V sub is less than V . For the prediction of fluidized bed density ( ρ bed ), a general correlation has been proposed in earlier work and is shown as ρ b e d = ( 1 ε m f ) ( ρ p ρ g ) [ 1 Y / false( 1 + 1.3 ( H / 2 + 4 A D 0.5 ) false( U g U m f false) 0.8 false) ] where ε mf is the bed voidage at the minimum fluidization state, ρ g is the gas density, ρ p is the density of solid particles, H is the height of the fluidized bed, A D is the area of each orifice on the gas distributor, U g is the superficial gas velocity, U mf is the minimum fluidization velocity, and Y is the correction factor for the Two-phase Theory of Fluidization. For Geldart Group A powders, the Y value is very close to 0.85 .…”
Section: Theorymentioning
confidence: 99%
“…Otherwise, V sub is less than V. For the prediction of fluidized bed density (ρ bed ), a general correlation has been proposed in earlier work 21 and is shown as…”
Section: Theorymentioning
confidence: 99%
“…The air dense medium fluidized bed (ADMFB) is a branch of the gas–solid bubbling fluidized bed. The technology is mainly used for coal beneficiation, relying on the prominent advantage of a relatively stable bed density distribution. With the global expansion of water scarcity, the dry separation method has attracted more and more attention, especially in China, India, Turkey, etc. During the separation process, ADMFB can effectively separate clean coal and gangue due to the density difference. , Upward air flow suspends medium particles to form a fluid-like separation bed with a certain density ρ bed . Ideally, coal with lower density ρ coal floats to the top zone and gangue with higher density ρ gangue sinks to the bottom .…”
Section: Introductionmentioning
confidence: 99%
“…4−6 During the separation process, ADMFB can effectively separate clean coal and gangue due to the density difference. 7,8 Upward air flow suspends medium particles to form a fluid-like separation bed with a certain density ρ bed . Ideally, coal with lower density ρ coal floats to the top zone and gangue with higher density ρ gangue sinks to the bottom.…”
Section: Introductionmentioning
confidence: 99%
“…The expansion rate of the emulsion phase is low, and to reduce the bed density, the proportion of the bubble phase needs to be increased accordingly. , However, if the proportion of the bubble phase is too large, then the bubbles are continuously merged and grown during the rising process, and the bed density fluctuates greatly, which is also not suitable for coal separation. Therefore, Dong et al introduced pulsating airflow into fluidized beds to form a pulsed gas–solid separation fluidized bed. , According to previous studies, pulsed fluidized beds can effectively inhibit the merger of bubbles, improving the fluidized quality of particles and optimizing a separation accuracy of −6 mm coal. …”
Section: Introductionmentioning
confidence: 99%