Abstract

Polymer extrusion is an energy intensive process, which is often run at less than optimal conditions. The extrusion process consists of gradual melting of solid polymer by thermal conduction and viscous shearing between a rotating screw and a barrel; as such it is highly dependent upon the frictional, thermal and rheological properties of the polymer. Extruder screw geometry and extrusion variables should ideally be tailored to suit the properties of individual polymers, but in practice this is rarely achieved due to the lack of understanding of the process. Here, in-process monitoring techniques have been used to characterise the thermal dynamics of the extrusion process. Novel thermocouple grid sensors have been used to measure melt temperature fields within flowing polymer melts at the entrance to an extruder die in conjunction with infra-red thermometers and real-time quantification of energy consumption. A commercial grade of polyethylene has been examined using three extruder screw geometries at different extrusion operating conditions to understand the process efficiency. Extruder screw geometry, screw rotation speed and set temperature were found to have a significant effect on the thermal homogeneity of the melt and process energy consumed.

Highlights

  • U.K. top 5 plastics processing countries in Europe, £19 billion accounting for 2.1% of GDP [source: British Plastics Federation]

  • Exploring the correlation between measurements made with the infra red sensor in the screw channel and thermocouple grid at the extruder die Colleagues: o Tim Gough o Steve Brook o John Wyborn o Ken Howell

  • Dependence of melt viscosity on the thermal dynamics High dependence on screw geometry

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Summary

Background

Aims: To facilitate efficient use of thermal energy in polymer processing plant operation. O Energy management tool: development and validation o On-line monitoring and control. O Application of novel process monitoring techniques and determination of effect of processing/material on specific energy consumption in extrusion

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