Scale lateral distance with , transverse distance with , lateral velocity with , and the normal velocity with . Balancing lateral pressure force with transverse viscous stress gives pressure scale . The ratio of inertia to that stress is , while lateral viscous derivatives are smaller by . The two stated smallness conditions therefore reduce the lateral equations to , . The normal component of balance of linear momentum gives at leading order; continuity remains . The no-slip, impermeable rigid plates require at both plate surfaces.
Integrating with those boundary values gives
Depth-integrated continuity has no normal boundary flux, so and away from the injection point.
Neglecting surface tension, the fluid free boundary has , and its normal velocity is the fluid velocity: . Any constant capillary pressure for a circular interface can instead be included in that spatially uniform boundary pressure. Conservation of injected volume gives . Hence
The logarithmic pressure singularity represents the ideal point source, which in a physical cell is replaced by a finite inlet. The formula is an exact radial solution of the depth-averaged model for either sign of , while .
Its robustness differs sharply between the signs. With viscous fluid inside a much less viscous exterior, injection displaces the less viscous phase and is stabilizing; suction draws the exterior into the viscous region and is prone to fingering. One can see this directly without relying on a slogan. Write the boundary as and its regular pressure perturbation as . Linearizing the constant-pressure condition gives . The perturbation radial velocity is then , and evaluation of the base velocity at the displaced boundary adds . Thus
Modes decay for injection and grow for suction. Accordingly the suction circle is a mathematically possible symmetric solution but generally an unstable prediction, failing before its formal collapse in a perturbed experiment. This is Stability of an interior Hele-Shaw blob under injection and suction.

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