A model was developed to determine the radiative heat transfer in bubb
ling fluidized beds taking the bubble and suspension contact at the wa
ll into account. The bubble radiation can be regarded as the heat exch
ange between two isothermal surfaces. The suspension radiation is desc
ribed between single particles of the near wall particle layer and the
wall during suspension contact at the wall. The two mechanisms partic
le convection and suspension radiation are simultaneous effects which
both results in a decrease of the temperature at the particle surface.
The time dependent particle surface temperature can be determined fro
m heat balances of the particle and at the particle surface which are
simultaneously influenced by convection and radiation. From this infor
mation the suspension radiation can be evaluated. The model results an
d experimental data were compared and a relatively good agreement was
found. The discrepancies are small and no systematic deviations were o
bserved. The model results show not only the expected influence of the
bed temperature on the radiative heat transfer but also a strong infl
uence of the particle diameter. Increasing particle diameter increases
the radiative heat exchange. The fluidizing velocity influences the r
adiation via the bubble volume fraction within the bed. Furthermore th
e radiation is effected by the wall temperature. The system pressure h
as a minor influence on the radiation by the pressure dependency of th
e particle convection. Since the application of the radiation model pr
esented here is rather complicated an empirical equation was developed
to determine the radiative heat exchange. This equation is easy to ha
ndle and represents the results of the complete model as well as all i
nfluences which are discussed here. This equation fits the experimenta
l results with a maximum deviation of 20%. The radiation model is veri
fied in a wide range of different parameters so that it includes not o
nly applications of pressurized fluidized bed combustion but includes
also other applications for example fluidized beds with metallic bed m
aterial.