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An In-line Melt Rheometer for Molten Plastics

Part 2: Dynamic Response Characteristics
  • B. I. Nelson , T. O. Broadhead , W. I. Patterson and J. M. Dealy
Published/Copyright: May 27, 2013
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Abstract

An in-line rheometer designed for use as a sensor for closed-loop control of melt processing operations has been previously described. This instrument can measure the true viscosity of a melt stream over a range of shear rates. In order to evaluate its performance in processing applications the rheometer was mounted on a twin-screw extruder. A chemical degradation process was used to introduce changes in the molecular weight distribution, and thus the viscosity of a polypropylene resin, and these changes were monitored using the rheometer. For rapid replacement of melt in the zone of controlled shear in the rheometer, flow simulations indicated that it would be advantageous to operate the rheometer in a cyclic mode. A stochastic process identification technique based on a pseudorandom binary signal was used to determine the parameters of a first-order plus deadtime model of the process. In order to estimate the portion of the system response due to rheometer dynamics, residence time distributions were measured both with and without the rheometer present. It was found that the rheometer has a dead time of about 6's and a first order time constant of less than 15 s. The response of the new instrument is thus significantly faster than than that of melt process rheometers now commercially available.


*** Mail address: Prof. J. M. Dealy, Department of Chemical Engineering, McGill University, 3480 University St., Montreal, QC, Canada H3A 2A7.

Received: 1993-9-27
Accepted: 1994-2-1
Published Online: 2013-05-27
Published in Print: 1994-09-01

© 1994, Carl Hanser Verlag, Munich

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