A mathematical model for the changes in molecular weight distribution
that occur when free-radical initiator is added to a blend of linear l
ow-density polyethylene and polypropylene during extrusion was develop
ed. Experimental verification employed a size-exclusion chromatograph
equipped with both differential refractive index detection and a solve
nt-evaporation interface to enable infrared detection. The model combi
nes two previously published models (a polypropylene degradation model
and a polyethylene modification model) using a single parameter: an i
nitiator partition coefficient. All of these models were shown to prov
ide excellent fits to new reactive extrusion data. However, with one o
f the initiators used, the polyethylene modification model required va
lues of initiator efficiency greater than unity. This result was also
recently observed in another study and may be due to localized variati
ons in peroxide concentration or to an inadequacy in the reactions spe
cified for polyethylene with this initiator.