Vorticity distributions in axisymmetric vortex rings produced by a piston–pipe apparatus are numerically studied over a range of Reynolds numbers,   $Re$ , and stroke-to-diameter ratios,
 $Re$ , and stroke-to-diameter ratios,   $L/D$ . It is found that a state of advective balance, such that
 $L/D$ . It is found that a state of advective balance, such that   $\unicode[STIX]{x1D701}\equiv \unicode[STIX]{x1D714}_{\unicode[STIX]{x1D719}}/r\approx F(\unicode[STIX]{x1D713},t)$ , is achieved within the region (called the vortex ring bubble) enclosed by the dividing streamline. Here
 $\unicode[STIX]{x1D701}\equiv \unicode[STIX]{x1D714}_{\unicode[STIX]{x1D719}}/r\approx F(\unicode[STIX]{x1D713},t)$ , is achieved within the region (called the vortex ring bubble) enclosed by the dividing streamline. Here   $\unicode[STIX]{x1D701}\equiv \unicode[STIX]{x1D714}_{\unicode[STIX]{x1D719}}/r$  is the ratio of azimuthal vorticity to cylindrical radius, and
 $\unicode[STIX]{x1D701}\equiv \unicode[STIX]{x1D714}_{\unicode[STIX]{x1D719}}/r$  is the ratio of azimuthal vorticity to cylindrical radius, and   $\unicode[STIX]{x1D713}$  is the Stokes streamfunction in the frame of the ring. Some, but not all, of the
 $\unicode[STIX]{x1D713}$  is the Stokes streamfunction in the frame of the ring. Some, but not all, of the   $Re$  dependence in the time evolution of
 $Re$  dependence in the time evolution of   $F(\unicode[STIX]{x1D713},t)$  can be captured by introducing a scaled time
 $F(\unicode[STIX]{x1D713},t)$  can be captured by introducing a scaled time   $\unicode[STIX]{x1D70F}=\unicode[STIX]{x1D708}t$ , where
 $\unicode[STIX]{x1D70F}=\unicode[STIX]{x1D708}t$ , where   $\unicode[STIX]{x1D708}$  is the kinematic viscosity. When
 $\unicode[STIX]{x1D708}$  is the kinematic viscosity. When   $\unicode[STIX]{x1D708}t/D^{2}\gtrsim 0.02$ , the shape of
 $\unicode[STIX]{x1D708}t/D^{2}\gtrsim 0.02$ , the shape of   $F(\unicode[STIX]{x1D713})$  is dominated by the linear-in-
 $F(\unicode[STIX]{x1D713})$  is dominated by the linear-in-  $\unicode[STIX]{x1D713}$  component, the coefficient of the quadratic term being an order of magnitude smaller. An important feature is that, as the dividing streamline (
 $\unicode[STIX]{x1D713}$  component, the coefficient of the quadratic term being an order of magnitude smaller. An important feature is that, as the dividing streamline (  $\unicode[STIX]{x1D713}=0$ ) is approached,
 $\unicode[STIX]{x1D713}=0$ ) is approached,   $F(\unicode[STIX]{x1D713})$  tends to a non-zero intercept which exhibits an extra
 $F(\unicode[STIX]{x1D713})$  tends to a non-zero intercept which exhibits an extra   $Re$  dependence. This and other features are explained by a simple toy model consisting of the one-dimensional cylindrical diffusion equation. The key ingredient in the model responsible for the extra
 $Re$  dependence. This and other features are explained by a simple toy model consisting of the one-dimensional cylindrical diffusion equation. The key ingredient in the model responsible for the extra   $Re$  dependence is a Robin-type boundary condition, similar to Newton’s law of cooling, that accounts for the edge layer at the dividing streamline.
 $Re$  dependence is a Robin-type boundary condition, similar to Newton’s law of cooling, that accounts for the edge layer at the dividing streamline.