A high pressure, high temperature Direct Asymmetric Reductive Amination (DARA) reaction was run in three different continuous reactor types; coiled tubes, horizontal pipes in series, and vertical pipes in series. The goal of this work was to design a continuous reactor scalable to large volumes needed for commercial scale manufacturing. With about 4000:1 substrate to dissolved catalyst ratio, the DARA reaction achieved about 90% conversion to desired product in 12 hours, about 8% conversion to undesired ketone, and about 95% ee, in batch and in all 3 types of continuous reactors. The 3 continuous reactors were compared on the basis of vapor liquid mass transfer rates, overall pressure drop, % liquid filled, and axial dispersion. Vertical pipes in series were selected for scale up to manufacturing because of scalability and vapor liquid mass transfer rates, although horizontal pipes had lower pressure drop and less potential for surging.