Meaning
Non-Newtonian fluid behavior characterized by decreasing apparent melt viscosity under increasing shear rates governs polymer fluid mechanics during high-velocity flow. Relying on shear thinning polymer rheology enables rapid mold cavity filling at manageable injection pressures without overheating the material bulk. The phenomenon ceases to offer processing advantages once flow velocity drops during packing and cooling phases, where viscosity rebounds sharply.
Viscosity Model
Mathematical representation of shear-dependent flow behavior utilizes the Carreau-Yasuda or Cross viscosity models. Quantifying shear thinning polymer rheology requires capillary rheometer testing across shear rates from one hundred to ten thousand reciprocal seconds.
Molecular Shear
Polymer chains in an unperturbed melt state remain randomly coiled and entangled, creating high resistance to physical flow. When forced through narrow runners and gates under high pressure, shear thinning polymer rheology occurs as polymer chains untangle and align parallel to the flow direction. This alignment reduces intermolecular friction, causing apparent viscosity to drop by up to two orders of magnitude at high shear rates.
Linear low-density polyethylene exhibits stronger shear thinning behavior than branched low-density polyethylene, enabling thinner wall sections to fill rapidly. Blending regrind polymer with virgin material alters the shear sensitivity curve, requiring adjustments to injection speed profiles. Datasheet melt flow rate values reflect zero-shear conditions and fail to predict high-speed flow performance.
Processing Gain
Lower viscosity at high shear rates reduces hydraulic pressure requirements during the injection stroke. Utilizing shear thinning polymer rheology allows processors to run lower clamp tonnage machinery without inducing part flash or incomplete filling defects. Decreased fill pressure reduces mechanical stress on mold cores and prolongs tool life.