Shear Rheology
Polymer melts exiting a slot die in extrusion coating follow a predictable mathematical description known as the findley power law when relating apparent viscosity to shear rate under steady isothermal conditions. Fluid behaviour departs from Newtonian linearity because polymer chains disentangle and align parallel to the flow direction under mechanical stress, causing the viscosity to drop as the shear rate increases. Extrusion coaters use this mathematical relationship to predict melt fracture thresholds and calculate pressure drops through the coating die manifold.
Accurate modelling prevents edge beads and thickness irregularities on high speed paperboard packaging lines.
Die Geometry
Die design engineers apply viscoelastic parameters to control the velocity profile across the entire slot width during liquid packaging board extrusion. Flow channels taper uniformly to compensate for wall drag and maintain a constant residence time for the polymer melt before deposition onto the moving substrate. Thermal degradation occurs when local shear rates exceed the safe operating window defined by the fluid limits.
Substrate adhesion relies on maintaining consistent melt temperature and pressure right at the nip roll.
Coating Weight
Finished packaging materials demand tight grammage control across the web to meet conversion specifications for folding cartons and liquid containers. Extruders adjust screw speed and line velocity simultaneously to maintain target coating thickness while accounting for neck-in phenomena at the edges. Process operators measure final coat weight continuously using beta transmission gauges to verify that polymer application matches production targets.
Uniform polymer deposition ensures grease resistance and heat seal integrity during subsequent carton forming operations.