Convective heat transfer in a particle packed tube is modeled in this
paper. Axial and radial dispersion are both included in the governing
equations. Results are compared with experimental data, and with previ
ously developed models that did not include axial dispersion. It is sh
own that heat transfer in the thermally developing region is affected
by axial dispersion when Peclet number is smaller than 10. Graphic res
ults are provided to show the importance of axial dispersion for vario
us Peclet numbers.