Meaning
Tooling designs for molten thermoplastics account for shear-rate dependent viscosity changes that occur as polymer melt moves through sprue, runner and gate sections. Operating a non-Newtonian flow injection mold requires matching runner dimensions and gate geometries to the shear-thinning characteristics of the specific polymer formulation. Boundary conditions limit these design considerations to shear rates between one hundred and one hundred thousand reciprocal seconds typical of commercial injection processing.
Viscosity Response
Apparent viscosity drops rapidly when shear rate increases during filling phase injection. Utilizing a non-Newtonian flow injection mold leverages this shear-thinning behavior to fill complex geometry sections without excessive hydraulic pressure requirements.
Tooling Optimization
Standard Newtonian fluid dynamics equations fail to predict pressure drop or fill patterns in thermoplastic tooling. Constructing a non-Newtonian flow injection mold involves rheological modeling that incorporates cross-WLF viscosity coefficients derived from capillary rheometer testing. Accurate channel sizing prevents excessive shear heating while maintaining sufficient flow velocity to fill thin wall sections before thermal freezing occurs.
Incorporating regrind material alters the shear response of the resin blend, requiring runner systems with wide processing windows to absorb batch-to-batch viscosity shifts. Datasheet melt flow rate values provide only single-point measurements, whereas proper mold design utilizes full viscosity curves across multiple shear rates and processing temperatures.
Process Control
Injection speed regulation directly controls shear rate within channels and gate orifices. Operating a non-Newtonian flow injection mold demands multi-stage injection velocity profiling to maintain uniform melt front velocity throughout cavity filling. Proper velocity control eliminates jetting defects and lowers internal stress levels in finished components.