The reactive coprocessing of scrap tires and heavy oil was carried out
at temperatures of 375, 400, 425, and 450 degrees C. The ultimate yie
lds from the following process cases were determined: scrap tires with
out oil, SAE 50 weight oil without scrap tire, and scrap tires in the
presence of SAE 50 weight oil. Kinetic constants were obtained for all
three cases. The values of activation energy showed that the coproces
sing of scrap tires and heavy oil is a more favorable reaction pathway
for decomposing these waste materials to more useful products than th
e pyrolysis of tires alone. The distillates produced by the processing
of these materials were analyzed using gas chromatography/mass spectr
oscopy. The analysis of the three cases showed that coprocessing scrap
tires and heavy oil yields more toluene compared to the pyrolysis of
the individual waste materials. Therefore, it was concluded that the c
oprocessing of scrap tires plus heavy oil occurs at a lower temperatur
e and produces higher-value products than the pyrolysis of scrap tire
without heavy oil.