1965
DOI: 10.1002/aic.690110335
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On a generalized expression for prediction of minimum fluidization velocity

Abstract: t i m e , sec. Fig. 3. Expansion of beds of glass beads. A-Reference I, glass beads, 70 to 80 mesh; eSS N 0.66; h,, = 14.2 cm.; hi = 26 cm.; diameter of the column = 50 mm. B-Reference 3, glass beads, 20 to 25 mesh; ess = 0.40; h,, = 23.8 cm.; hi = 51.8 cm.; diameter of the column = 35 mm. -Piston flow. ----Complete mixing according to Equation (3). -.-.-.-Linearized model for complete mixing according to Equation (5). diagrams within theoretical curves for piston flow and complete mixing models. NOTATION h h,… Show more

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Cited by 30 publications
(7 citation statements)
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“…For reliability sake the correlation developed from pressure drop is compared with some popularly used correlations (Wen and Yu, Leva, Narshiman) [26,33,34] and the statistical results are included in Table 3. These results reveal that the prediction from the proposed correlation (Eq.…”
Section: Resultsmentioning
confidence: 99%
“…For reliability sake the correlation developed from pressure drop is compared with some popularly used correlations (Wen and Yu, Leva, Narshiman) [26,33,34] and the statistical results are included in Table 3. These results reveal that the prediction from the proposed correlation (Eq.…”
Section: Resultsmentioning
confidence: 99%
“…where d P is the particle diameter in feet [18]. The procedure was repeated for all the particle sizes and materials used in each of the tapered columns.…”
Section: Methodsmentioning
confidence: 99%
“…Particulate sphericity and bed voidage can be calculated by Eqs. (4) and (5) [14], the sphericities of 51 lm quartz sand and FCC particles are 0.443 and 0.597, and their corresponding voidage is 0.648 and 0.526, respectively.…”
Section: Fluidization Behaviors Using Fcc Particlesmentioning
confidence: 99%