THESIS
2012
xiii, 107 leaves. : ill. ; 30 cm
Abstract
Polymer extrusion, an important polymer processing technique, is a continuous process,
during which material property, machine variables and process variables interact with
each other in determining the final product quality. Control of key process variables
such as melt pressure and barrel temperatures with high precision is essential to achieve
a good product quality in extrusion process.
In this thesis, an overall control system is proposed for the extrusion process with two
independent control loops, a single-input-single-output (SISO) control loop for the melt pressure at die output and a multi-input-multi-output (MIMO) control loop for the barrel
temperatures. The dynamics of the melt pressure and barrel temperatures are analyzed
before the controller construction. It is f...[
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Polymer extrusion, an important polymer processing technique, is a continuous process,
during which material property, machine variables and process variables interact with
each other in determining the final product quality. Control of key process variables
such as melt pressure and barrel temperatures with high precision is essential to achieve
a good product quality in extrusion process.
In this thesis, an overall control system is proposed for the extrusion process with two
independent control loops, a single-input-single-output (SISO) control loop for the melt pressure at die output and a multi-input-multi-output (MIMO) control loop for the barrel
temperatures. The dynamics of the melt pressure and barrel temperatures are analyzed
before the controller construction. It is found that the melt pressure dynamics is
nonlinear and time-varying while the extruder barrel temperatures are of nonlinear, slow
response characteristics with different zones highly coupled. Advanced control
algorithms are adopted in this project to control these key variables. Experimental
results demonstrate that fast response, near-zero overshoot and precise tracking
performance could be achieved through the proposed control strategies. The robustness
of the control system is also verified by investigating the variations of operation
conditions with respects to different materials and set-points.
The benefits of the proposed controllers can be reflected by product quality, which can
be indicated by the product diameter variation. Comparing with commercial controller,
the reduction of process variables variation brings significant improvement on product
quality. The robustness and effectiveness of the proposed controllers are reflected under
different operation conditions and materials as well.
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