Meaning
The actual resistance to flow of a polymer melt, corrected for non-Newtonian behavior and entrance-exit pressure losses, defines the intrinsic flow resistance of the material. Rheologists calculate true viscosity to ensure accurate modeling of polymer behavior during high-pressure molding and extrusion operations. This fundamental property is independent of the test geometry or instrument used for the measurement.
Failing to utilize the corrected value leads to underestimating the clamping force needed in injection molds.
Correction Method
Rabinowitsch and Bagley corrections are applied to capillary rheometer data to eliminate errors introduced by fluid elasticity and shear-thinning. To obtain the true viscosity, the raw pressure drop must be adjusted to account for the energy consumed in organizing the polymer chains as they enter the capillary die. This step separates boundary effects from the bulk shear flow.
Measurement Technique
Multi-die capillary rheometry allows for the simultaneous measurement of entrance pressure losses across different land lengths. By analyzing the resulting Bagley plot, the practitioner isolates the pressure drop associated with the fully developed flow from the exit effects. This correction yields a true viscosity value that can be used across different software platforms for mold design.
Using uncorrected data can lead to tooling that causes part defects due to unexpected pressure drops during the filling phase. It is therefore standard practice to perform these corrections for any high-precision molding application.
Engineering Value
Numerical simulations of mold filling rely on these corrected viscosity profiles to generate accurate velocity fields. Under high-shear conditions, the discrepancy between apparent and true viscosity is pronounced. This makes the correction step vital for high-speed manufacturing processes where precision is paramount.