The unsteady flow of a homogeneous viscous fluid past a straight circular cylinder (radius l*) confined between two infinite parallel plates (a distance d* apart) relative to a rapidly rotating frame is considered. The cylinder is impulsively started from rest to a uniform velocity. The unsteady form of the boundary-layer equations for a rotating fluid is used to examine the flow Rossby number Ro∼O(E1/2), where E≪1 is the Ekman number. A range of values of the non-dimensional parameter N=lE1/2/Ro (where l=l*/d*) is considered. For 0⩽N<1, the flow pattern resembles that of the non-rotating case (N=0). Initially, the wall shear around the cylinder is positive everywhere. After a time, flow reversal begins at the rear stagnation point and then the position of zero wall shear moves upstream, towards the front stagnation point. The boundary-layer thickness in the region of reversed flow grows with time until a singularity/eruption at a point in the flow occurs. The boundary-layer equations are written in terms of Lagrangian coordinates in order to numerically investigate the finite-time singularity for 0⩽N<1. The flow close to the rear stagnation point is also examined in detail for a range of values of N and results are compared with the large-time asymptotic forms for the growth of the displacement thickness. The analysis suggests the displacement thickness in this region grows exponentially with time, for certain ranges of N. For 0<N<1, the displacement thickness grows exponentially with time in a manner similar to the non-rotating case. For N>1, the wall shear remains positive for all time. However, for 1⩽N<2, the displacement thickness of the boundary layer close to the rear stagnation point again grows exponentially with time. For 2<N<3 the flow close to the rear stagnation point also grows exponentially with time, although the form of solution differs from that for 0⩽N<2. For N>3, the solution tends to a truly steady limit, consistent with previous studies on the steady problem.