The flow through a axially rotating pipe is examined using the open-source code OpenFOAM for both standard eddy-viscosity models (Spalart-Allmaras & k − ω SST) and a low-Reynolds number Elliptic Blending Reynolds Stress Model with a homogenous turbulent dissipation rate equation. Corrections to the length-scale determining equation for rotation, based upon the work of Hellsten et al. (1998), are evaluated for both the SST and EB-RSM models. It is shown that for models with or without a rotation correction, the EB-RSM offered improved results over the SST model, better capturing the level of turbulence suppression and the parabolic circumferential velocity profile. A clear improvement to both the SST and EB-RSM models is observed when a Richardson correction is applied to the length-scale determining equations, resulting in much closer agreement to the experimental data. The results for the EB-RSM with this correction are in good agreement with previous studies and further improvements to the turbulent diffusion model would likely improve the correlation to the experiment even further. The performance of the SST model is better than expected although the reliance of both models on the Richardson correction suggests further work is needed to thoroughly assess the formulation of such corrections for a wider range of flows.