A new mathematical model has been developed to analyze the entire flow fiel
d of a single screw extruder under steady-state conditions. Intended as a r
ational design tool for practising engineers in the polymer processing indu
stry, the model contains no partial differential equations and hence does n
ot require the use of numerical solution techniques. To achieve generality,
a generic approach is proposed and has been adopted in the derivation of g
overning algebraic equations from general conservation laws covering channe
l geometry, polymer flow speed, equivalent radius in a pipe, material prope
rties, power consumption and heat transfer. The model makes no use of empir
ical factors or correlation. The validity of the new model has been assesse
d by comparison with published experimental results. Good agreement was ach
ieved with respect to its ability to predict (a) the solid-bed width profil
e; (b) the axial pressure profile and (c) the temperature and pressure of t
he melt pool at the extruder exit. Furthermore, the model can predict other
information including the solid-bed velocity in the axial direction and th
e power consumption. The work has demonstrated the potential of a fast trac
k approach to designing helical extruder screws, while maintaining a level
of accuracy comparable with more complex 3D models but without the penalty
of computational efforts.