1973
DOI: 10.1002/cjce.5450510324
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Vertical pneumatic conveying: An experimental study with particles in the intermediate and turbulent flow regimes

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1976
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1976
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Cited by 2 publications
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“…For dense phase conveying the slip velocity between gas and solid is necessarily higher than that corresponding to minimum fluidization. The equation for predicting the tránsition from dense phase flow (fluidized bed flow) to moving bed flow may be derived by equating the slip velocity iii vertical pneumatic conveying with the slip velocity at incipient fluidization (Leung et al, 1969). At this transition the voidage in the tube is equal to the voidage at minimum fluidization.…”
Section: Flow Patterns In Vertical Conveyingmentioning
confidence: 99%
“…For dense phase conveying the slip velocity between gas and solid is necessarily higher than that corresponding to minimum fluidization. The equation for predicting the tránsition from dense phase flow (fluidized bed flow) to moving bed flow may be derived by equating the slip velocity iii vertical pneumatic conveying with the slip velocity at incipient fluidization (Leung et al, 1969). At this transition the voidage in the tube is equal to the voidage at minimum fluidization.…”
Section: Flow Patterns In Vertical Conveyingmentioning
confidence: 99%
“…The transition from fluidized flow to a packed bed in vertical pneumatic conveying is entirely analogous to the transition from fluidized flow to packed-bed flow in vertical hydraulic conveying. The latter transition we have discussed elsewhere (Leung et al, 1969), and a method for predicting the transition in hydraulic conveying was described. The same method may be used for predicting this transition in pneumatic conveying.…”
mentioning
confidence: 99%