In the most commonly used scale-up method of plasticating extruder screws, the screw channel depth is increased by the square root of the diameter ratio while the screw RPM is decreased by the square root of the diameter ratio such that the output rate increases proportionally to the square of the diameter ratio. This scale-up method, largely based on the pumping function of the screw, often leads to a higher melt temperature, a higher screw horsepower consumption per unit output rate and an inferior melt quality from the larger diameter screw. Analysis of the common scale-up method reveals that, although the shear rate in the melt is kept constant, the average residence time and the peripheral screw speed are increased for the larger diameter screw. Our recent study on the melting mechanism also reveals that the melting capacity increases less than the pumping capacity. A detailed examination of the common scale-up method in this paper shows that the pumping capacity and the solid conveying capacity increase more than necessary while the melting capacity increases insufficiently.
[1]
Z. Tadmor,et al.
Fundamentals of plasticating extrusion. I. A theoretical model for melting
,
1966
.
[2]
S. Middleman,et al.
The calculation of screw characteristics for the extrusion of non‐Newtonian melts
,
1965
.
[3]
C. Chung,et al.
Maximum pressure developed by solid conveying force in screw extruders
,
1975
.
[4]
J. Watson,et al.
Analytical melting model for extrusion: Melting rate of fully compacted solid polymers
,
1982
.
[5]
C. Chung,et al.
Analytical melting model for extrusion: Stress of fully compacted solid polymers
,
1983
.