Influence of funnel-shape internals on hydrodynamics and mass transfer in internal loop three-phase fluidized bed
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Influence of funnel-shape internals on hydrodynamics and mass transfer in internal loop three-phase fluidized bed
CIESC JournalIssue 3, (2007)
作者机构:
华南理工大学环境科学与工程学院
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Online First:05 March 2007,
Published:05 March 2007
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韦朝海 李磊 吴锦华 吴超飞 吴景雄. Influence of funnel-shape internals on hydrodynamics and mass transfer in internal loop three-phase fluidized bed[J]. CIESC Journal, 2007, (3).
DOI:
韦朝海 李磊 吴锦华 吴超飞 吴景雄. Influence of funnel-shape internals on hydrodynamics and mass transfer in internal loop three-phase fluidized bed[J]. CIESC Journal, 2007, (3).DOI:
Influence of funnel-shape internals on hydrodynamics and mass transfer in internal loop three-phase fluidized bed
The effects of funnel-shape internals on hydrodynamics and mass transfer in an internal loop three-phase fluidized bed were investigated. Three different kinds of internals were designed which were setup on the top of draft-tube in terms of horizontal angle and outer diameter
and gas hold up
liquid mixing time
liquid circulation velocity and mass transfer coefficient were measured respectively.It was shown that the riser gas holdup and mass transfer coefficient increased by 10% and 15% than that without such an internal
liquid mixing time decreased by 10% to 25%.When the superficial gas velocity was less than 0.5 cm·s-1
liquid circulation velocity increased with the setup of such internals.Liquid circulation velocity decreased when the superficial gas velocity was above 0.5 cm·s-1.In addition
the variation of structural parameters of funnel-shape internals had significant effects on hydrodynamics and mass transfer.
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