The relationship between the one dimensional Taylor—Aris model and the more detailed diffusion model for the steady state behavior of a tubular reactor is studied for the case of laminar flow and a first order reaction. It is shown that: (1) the Taylor—Aris model is valid provided that ka 2/3·8 2 D < 1; (2) the mean concentration computed using the Taylor—Aris model should be identified as the mean in the plane, C m , and the net flux across any plane perpendicular to the axis of the reactor is C m −[( a 2 U 2/48 D) + D] (∂ C m /∂ z); for large N pe the inlet condition. C m (0) = 1−( ka 2/ D)(1/48+1/ N 2 Pe ), seems to yield better results than the Wehner—Wilhelm boundary condition; and the zero gradient boundary condition is not the proper one to use at the outlet end of the reactor. It seems to be more appropriate to simply truncate a semi-infinite solution.