Recent studies ͓Lathrop et al., Phys. Rev. A 46, 6390 ͑1992͒; Lewis et al., Phys. Rev. E 59, 5457 ͑1999͔͒ on Taylor-Couette flow, where the inner cylinder is rotating and the outer one is at rest, show that, despite earlier predictions ͓Wendt, Ing. Arch. 4, 557 ͑1933͒; Tong et al., Phys. Rev. Lett. 65, 2780 ͑1990͔͒, the non-dimensional torque (GϭT/ 2 L) does not follow a fixed power-law scaling ͑i.e., GϳRe ␣ , where ␣ is a constant value͒ for 800ϽReϽ1.23ϫ10 6 . Here, we perform simultaneous flow visualization and high precision torque measurements of the same flow configuration using a Haake RS-75 Rheometer to establish if this is also true in the lower Reynolds number range (ReϽ800). Results show that, although ␣ varies with the Reynolds number, it can be approximated reasonably well with a constant value ␣ϭ1 for Re/Re c Ͻ1 and ␣ϭ1.5 for 1.5 ϽRe/Re c Ͻ6.32. The latter finding is in good agreement with that of Wendt ͓Ing. Arch. 4, 557 ͑1933͔͒. A possible explanation for the differences with the results of earlier studies is provided in this paper.