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Wall to fluid heat transfer in liquid fluidised beds: Part 2
Author(s) -
Asmund B. W,
Smith J. W.
Publication year - 1967
Publication title -
the canadian journal of chemical engineering
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.404
H-Index - 67
eISSN - 1939-019X
pISSN - 0008-4034
DOI - 10.1002/cjce.5450450307
Subject(s) - heat transfer , heat transfer coefficient , thermal conduction , thermodynamics , heat flux , materials science , convection , convective heat transfer , mechanics , porosity , particle (ecology) , film temperature , fluidization , turbulence , fluidized bed , nusselt number , composite material , reynolds number , geology , physics , oceanography
Wall to fluid heat transfer coefficients and radial temperature profiles have been obtained for beds of hydrodynamically similar spheres fluidized with water in a 2.058 inch pipe at a constant heat flux. From packed bed to open pipe conditions, heat transport occurs mainly by turbulent mixing, although conduction through the particles and possibly particle convection have some effect at low porosities. This result contradicts a previously published prediction based on model calculations using erroneous temperature profiles (24) . The model predicts a minor role for particle convection when appropriate temperature profiles are used. A series model based on the observed shift of thermal resistance from the wall region to the bulk of the bed with decreasing porosity is used to correlate heat transfer coefficients. The shift in resistance largely accounts for the maximum in heat transfer coefficient plots.