Back to the convection heat transfer problem... Solutions to the boundary layer equations are of the form: =,） dP" where: =0 for flat plate x* -小器 .Rewrite the convective heat transfer coefficient t 一k 6 T-T -ki h, 9 T。-I T,-T. T-T。 T-T. L kr 「a Define the Nusselt number as: Nu .o.Back to the convection heat transfer problem… • Solutions to the boundary layer equations are of the form: • Rewrite the convective heat transfer coefficient • Define the Nusselt number as:                * * * * * * * * * * * * , ,Re ,Pr, , ,Re , where : 0 for flat plate dx dP T f x y dx dP dx dP u f x y L L L T T L y T T T T T T k T T y T k T T q h s y s s s f s y f s x x                                         0 0 0 * * *           y f x y T L k h            * * * 0 * * ,Re ,Pr, * dx dP f x y T L y Nu