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Advances in Fluidized Bed Heat Transfer 1
Heat Transfer to Banks of Immersed Tubes
9 other sections not shown
Amundson assumed axial bed diameter bed height bed-to-surface heat transfer behaviour Botterill bubble diameter bubble phase Bukur calculated catalyst Chavarie Chem Chemical Combustion convective correlation dead zone dense phase gas density dimensionless dimensionless group distributor plate effect elutriation emulsion phase entrainment experimental fluid bed fluid-bed Fluidized Bed Combustion Fluidized Bed Reactors fluidized-bed reactor fluidizing velocity Fokker-Planck equation fraction freeboard region Gas Distributor Gas Fluidized Beds gas-solid Geldart grid heat transfer coefficient heat transfer surface Horizontal Tube immersed increase interphase Keairns Kunii Levenspiel mass transfer measurements minimum fluidization nozzle obtained operating order reaction orifice packed bed parameter Powder predictions pressure drop ratio profiles rate constant reactant reaction reactor model Saxena shown in Figure solid particles steady-state superficial gas velocity Symp thermal thermal conductivity tion tuyeres two-phase type of distributors values variables vertical voidage volume Werther Zabrodsky zone