Coupled heat transfer between laminar forced convection along and conductio
n inside a flat plate wall is theoretically studied. The laminar convective
boundary layer is analyzed by employing the integral technique. The energy
equations for the fluid and the plate wan are combined under the condition
of the continuity in the temperature and heat flux at the fluid-solid inte
rface. The analysis results in a simple formal solution. Expressions have b
een obtained for calculating local Nusselt number, wall heat flux and tempe
rature along the plate, all are functions of the local Brun number, Br-x, w
hich is a measure of the ratio of the thermal resistance of the plate to th
at of the convective boundary layer. The results indicate that for Br-x gre
ater than or equal to 0.15, neglecting the plate resistance will results in
an error of more than 5% in Nusselt number. Comparison of the present solu
tion with other previous studies has been made. The solution may be of a co
nsiderable theoretical and practical interest.