ANALYSIS OF SIMULTANEOUS RADIATIVE AND CONDUCTIVE HEAT TRANSFER IN FLUIDIZED BEDS
- 1 January 1981
- journal article
- research article
- Published by Taylor & Francis in Chemical Engineering Communications
- Vol. 9 (1-6) , 255-271
- https://doi.org/10.1080/00986448108911027
Abstract
In the bubbling regime of operation for fluidized beds, the major mechanism for heat transfer is transient conduction to periodic packets of densely packed particles at the heat transfer surface. The well known Mickley and Fairbanks model, with various subsequently proposed modifications, adequately describes this transient conduction mechanism. However, no adequate theory exists for heat transfer in high-temperature fluidized beds where radiative contribution becomes significant. Analysis of the radiative contribution is complicated by the nonlinear interaction of radiation with conduction/convection. This paper describes a differential formulation of the combined radiative/ conductive heat transfer process. The discrete flux method used by Churchill et al. for radiative transport in heterogeneous media is applied here to the problem of transient heat transfer to packets in fluidized beds. Packets are modeled as radiatively participating media with absorption, scattering, and emission of radiation. Simultaneous solution of the governing differential equations for temperature and forward and backward radiation fluxes permits calculation of instantaneous heat flux at the heat-transfer surface. Radiative transfer during bubble contact is added as a time-weighted contribution. Using experimental data on radiative cross sections (from packed media experiments) and experimental data on packet residence times (from fluidized bed experiments), the combined conductive/radiative heat transfer to packets was obtained for examples of fluidized beds at different fluidizing velocities and wall temperatures. The analytical results indicate that the relative importance of radiation is affected by particle size, average packet residence time, and the radiative attenuation cross sections. For operating conditions representative of fluidized bed combustion, the model estimates a 10 to 20 percent contribution by radiation to the total heat transfer. Comparison to limited experimental data from the literature shows reasonable agreement.Keywords
This publication has 15 references indexed in Scilit:
- Emulsion phase residence time and its use in heat transfer models in fluidized bedsAIChE Journal, 1980
- Local Heat Transfer Coefficients around Horizontal Tubes in Fluidized BedsJournal of Heat Transfer, 1980
- A model of heat transfer in gas fluidized bedsInternational Journal of Heat and Mass Transfer, 1975
- Mechanism of bed-wall heat transfer in a fluidized bed at high temperaturesChemical Engineering Science, 1974
- An analysis of the conductive and radiative heat transfer to the walls of fluidized bed combustorsInternational Journal of Heat and Mass Transfer, 1974
- Heat transfer to objects immersed in fluidized bedsPowder Technology, 1973
- Bed to wall radiation heat transfer in a gas-solid fluidized bedChemical Engineering Science, 1969
- Study of radiative heat transfer in a fluidized bedJournal of Engineering Physics and Thermophysics, 1968
- Effects of Solid Thermal Properties on Heat Transfer to Gas Fluidized BedsIndustrial & Engineering Chemistry Fundamentals, 1964
- Heat transfer between fluidized‐solids beds and boundary surfaces—correlation of dataAIChE Journal, 1958