Abstract
A mathematical model for the two-dimensional flow field of power-law fluids in a screw extruder is developed and used to calculate screw characteristics, residence time distributions, delay times, and a weighted average total strain of fluid elements. The dependence of these variables on fluid properties and operating variables is presented and discussed. Experiments were performed with Newtonian and strongly non-Newtonian fluids which are in very good agreement with the predictions of the theory. © 1974, American Chemical Society. All rights reserved.
Cite
CITATION STYLE
Bigg, D., & Middleman, S. (1974). Mixing in a Screw Extruder. A Model for Residence Time Distribution and Strain. Industrial and Engineering Chemistry Fundamentals, 13(1), 66–71. https://doi.org/10.1021/i160049a013
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