Shear thinning
Non-Newtonian fluid behavior occurs when the apparent viscosity of a coating colour decreases under applied mechanical force during high-speed blade application. Pseudoplastic rheology dictates the operational limits of pigment suspension flow through metering systems on paper machines. Polymer chains align in the direction of shear during transfer from the applicator roll to the moving web.
Viscosity drops by several orders of magnitude as the shear rate climbs from static conditions to ten thousand reciprocal seconds. Coating thickness remains uniform across the web width only when this structural breakdown happens predictably inside the nip.
Dispersion stability
Pigment slurries maintain suspension through electrostatic repulsion and steric hindrance before hydrodynamic forces take over at the coating head. Clay and calcium carbonate particles agglomerate without sufficient hydrodynamic control during storage in mill tanks. High shear rates force entangled binder molecules to disentangle and release trapped water into the free phase.
Fluid resistance drops sharply because orientation reduces internal friction among mineral platelets. Water retention values govern how rapidly the released aqueous phase penetrates the raw paper stock beneath. Uneven dewatering creates binder migration defects that ruin print gloss and surface smoothness.
Flow response
High shear viscosity determines whether a metered film splits cleanly without creating orange peel or blade streaks on coated papers. Low shear viscosity prevents sedimentation in storage vessels and feed lines before the mixture reaches the application station. Excessive resistance causes high mechanical drag, motor overload, and web breaks at industrial operating speeds.
Formulators adjust coater runability by modifying binder ratios and adding associative thickeners to shift the onset of viscosity reduction. Finished print quality depends on this precise balance between station stability and rapid flow under mechanical stress.