Why the liquid slows down even though the pull stays the same
The driving force comes from the curved liquid surface at the leading edge of the flow. Surface tension tries to minimize that surface, and the resulting pressure difference — the capillary pressure — pushes liquid into the channel. The resisting force is viscous friction between the moving liquid and the channel walls. As liquid advances, more wall becomes wetted, so the friction grows even though the capillary pull stays roughly constant. The competition between a steady pull and a growing drag is what produces the familiar slowing: penetration length rises with the square root of time rather than in a straight line.
The rough-wall experiments make the timing of this balance concrete. Using rectangular glass-and-polymer channels, researchers found that contact-angle effects dominate the motion only early on; for their materials and fluids, those effects became negligible after about one second, leaving viscous behavior in charge [3]. That gives a useful rule of thumb: the capillary pull matters most at the start, and viscosity increasingly sets the pace afterward.
When the channel walls bend or catch the liquid
In very thin, deformable channels, the capillary pressure can actually squeeze the walls inward. A modeling study of a cylindrical elastic microchannel found that this inward deflection does not change the basic square-root scaling in either the early inviscid stage or the later viscous stage, but it does reduce the coefficient — the flow is slower than it would be in a rigid channel [2]. The same study reports a striking consequence at the endpoint: elasticity greatly raises the final equilibrium height the liquid reaches, and softer walls suppress the long-time oscillations in penetration length [2]. So flexibility mostly reshapes how far the liquid ultimately climbs and how smoothly it settles, rather than rewriting the underlying tug-of-war.
Roughness works differently. Sharp defects on the walls can cause the contact line to pin and then depin — the liquid edge sticks briefly, then jumps forward. In the rectangular rough channels studied, these events lowered the effective contact angle even at high aspect ratios, and channels with low aspect ratios showed the smallest effective contact angles alongside the largest effective friction coefficients [3]. In plain terms, geometry and surface texture can tune both sides of the balance at once: how strongly the liquid is pulled and how much drag it feels.
Adding an outside push to beat viscous drag
Because highly viscous liquids intrude slowly, one practical route is to add a force beyond capillarity. In experiments on viscous underfill flow between parallel plates, raising an applied electric potential to 500 V increased flow length by 45% compared with purely capillary flow [1]. Making the viscous liquid more polar by adding NaCl produced a 20–41% gain in flow length at 500 V versus 0 V for glycerol mixtures containing 0.5–4% salt [1]. The proposed explanation is that the field acts across the fluid and the fluid's permittivity rises, effectively supplementing the capillary pull [1]. Simulations matched the measurements closely, within about 4–7% at the time steps checked [1].
This is a case where the balance is deliberately tilted rather than left to surface tension and viscosity alone. It also shows the limit of the simple picture: when viscosity is high enough to make capillary-driven flow sluggish, an external field can restore speed without changing the channel itself.
What the balance means for designing a microchannel
The practical lesson is that intrusion speed is set by the ratio of capillary driving pressure to viscous resistance, and that ratio can be adjusted from several directions. Smooth, rigid, high-aspect-ratio channels favor predictable square-root filling; rough walls introduce pinning that can help or hinder depending on the surface [3]. Elastic walls slow the viscous-stage flow but can dramatically raise the final fill height and calm oscillations [2]. And where viscosity dominates, an electric field can add meaningful extra penetration [1].
One boundary on all of this: the evidence here concerns liquid intrusion and capillary rise in channels and between plates. A separate study of bubbles flowing in microchannels examines how viscosity, inertia, and capillarity set a bubble's sideways position and the resulting pressure drop [5], which is a different question from how far a liquid front advances. Likewise, a study of curved viscous fibers with surface tension addresses fiber spinning rather than channel filling [4], so it does not bear directly on microchannel intrusion. For channel design, the useful takeaway is that the capillary-versus-viscous balance is the baseline, and wall texture, wall flexibility, and external fields are the levers that shift it.
Sources used in this answer
Electric field and viscous fluid polarity effects on capillary-driven flow dynamics between parallel plates
At 500 V, viscous underfill flow length between parallel plates rose 45% over capillary flow, and adding 0.5–4% NaCl to glycerol raised flow length 20–41% at 500 V versus 0 V, with simulations matching experiments within 4–7%.
Elasto-capillary modulated filling dynamics in deformable microchannels
In a deformable cylindrical microchannel, inward wall deflection from capillary pressure leaves the inviscid and viscous Washburn scaling unchanged but lowers the Washburn coefficient, greatly raises the equilibrium height, and softer walls suppress long-time penetration oscillations.
Capillary Flow Dynamics in Composite Rectangular Microchannels with Rough Walls
In rectangular rough-walled microchannels, low aspect ratios gave the smallest effective contact angles and largest effective friction coefficients, pinning/depinning at wall defects reduced the effective contact angle, and contact-angle effects became negligible after about one second.
Dynamics of curved viscous fibers with surface tension
A slender-body asymptotic framework incorporating surface tension yields leading-order mass and momentum balance laws for curved viscous fibers, with numerical study of surface tension, viscosity, gravity, and rotation effects.
Bubbles dynamics in microchannels: inertial and capillary migration forces
For a train of bubbles in a microchannel, inertia, viscosity, and capillarity together set the transverse equilibrium position, velocity, and pressure drop, with surfactants and bubble deformation also affecting migration.
