A spherical clean bubble with negligible internal dynamic viscosity has zero tangential traction and permits tangential slip. In the creeping-flow, negligible-deformation limit its drag is , versus for a no-slip rigid sphere.
A spherical clean bubble with constant gas mass density and prescribed dissolution law obeys . With negligible gas dynamic viscosity, instantaneous terminal velocity is . Eliminating time yields the displayed radius-height relation and maximum rise . This uses an instantaneous force balance; a literally constant speed during shrinkage instead gives linear in height. The Reynolds number must remain small for the Stokes flow drag model to apply.
For a clean inviscid bubble a distance below a gravity-restored approximately flat free surface, the surface displacement scales as . Zero normal velocity and zero tangential traction are imposed to leading order by an opposite normal image Stokeslet at distance from the bubble. Its incident velocity is , which gives the displayed correction at fixed buoyancy. The image can be represented by a same-radius inviscid drop of density in liquid of density . Its deformation-producing strain is , so the leading fractional capillary deformation is ; small Bond number is the conventional stronger sufficient criterion.
A buoyantly rising inviscid bubble in otherwise quiescent unbounded liquid has an exterior Stokeslet with . Its tangential traction vanishes on the sphere. The dynamic normal traction is , while the hydrostatic normal-traction variation is . Their dipoles cancel at the terminal velocity, leaving a constant total normal stress compatible with uniform gas pressure even when surface tension is zero. This is an exact spherical solution in the stated Stokes model, not a proof of shape stability under arbitrary perturbations.

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