Polymer Engineering and Science · 1976 · 63 citations · 17 references
EngineeringMaterials EngineeringMaterials SciencePolymer EngineeringPolymer MaterialsRheologyFlow BehaviorMelt RheologyPolymer ProcessingPolymer RheologyRheological ModelingViscous FlowMultilayer Plastic FilmsPolymer MeltsPressure DropProcessing ConditionsRheological PropertiesShear RateShear StressVolumetric Flow Rate
Abstract Multilayer flat film coextrusion was studied, both experimentally and theoretically. For the experimental study, a sheet‐forming die with a feedblock was designed, and plastic films of three and five layers were coextruded. The die was provided with three pressure transducers in the axial direction in order to determine the pressure gradient in the die, allowing the determination of the reduction in pressure drop when different combinations of two polymer melts were coextruded. Polymers used for coextrusion were: (1) low density polyethylene and ethylene‐vinyl acetate; (2) low density‐polyethylene and high density polyethylene; (3) low density polyethylene and polystyrene. For the theoretical study, the z ‐component of the equations of motion for steady fully‐developed flow were solved using a power law non‐Newtonian model, Comparisons were made between the experimental and the theoretically predicted volumetric flow rates. Predictions of the velocity distributions, shear rate profiles, and shear stress distributions were made as functions of the processing conditions and the rheological properties of the individual polymers concerned.
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Instability due to viscosity stratification
Chia‐Shun Yih · Journal of Fluid Mechanics · 1967 · 736 citations
Rheology in polymer processing
F.N. Cogswell · Journal of Non-Newtonian Fluid Mechanics · 1977 · 680 citations
Helical Flow of General Fluids
Bernard D. Coleman, Walter Noll · Journal of Applied Physics · 1959 · 101 citations