As noted previously, this does allow classical analytical solution. There must always be temperature gradients if the heat flux is constant or no heat can flow. The outlet temperature gradient depends mainly on the fluid properties and the L/D ratio, but will always exist.
I mean here (concept of local temperature difference, is difference between the surface and fluid temperature(or bulk fluid temperature)) the difference between the max temperature (wall) and the min temperature in the fluid at the same isosurface or plane (cross section 3D pipe).