Virgin linear low-density polyethylene was subjected
to pyrolysis
in a fluidized bed reactor pilot plant segmented into three heating
zones with both sand and Magnofil BT 80 catalyst as bed materials.
The pyrolysis oil and wax products were extracted at an average bed
temperature of 600 and 700 °C. The oil yield decreased between
600 (8.7 wt %) and 700 °C (8.1 wt %) in an inverse relationship
with the reaction time (358 and 384 min, respectively). This was attributed
to an increase in the vibration of the polyolefin polymer matrix as
a result of the absorbed thermal energy with an increase in temperature.
The experiments performed at 700 °C showed no wax formation but
high yields of gaseous products and oils, which are more lucrative
in managing accumulated plastic waste, of which polyethylene constitutes
large proportions, via thermochemical conversion technologies. The
estimated calorific value at 600 °C was 45.5 MJ kg–1, which is in the acceptable range for both diesel and gasoline fuel
market specifications. The sulfur content in the pyrolysis oil was
estimated to be 0.013% and was not affected by changes in the temperature
of the fluidized reactor. However, desulfurization will be required
in the future to obtain oil within acceptable ranges of clean fuels.
In addition, to support this work’s results in obtaining fuels
from such feedstock materials, the fuel range hydrocarbons were also
analyzed. The diesel fuel hydrocarbon range (C10–C19) was between 37 and 60% in the pyrolysis oils examined.
The results determined experimentally from the pilot-plant work herein
are quite promising for sustainable fuel integration plans in the
near future with existing petroleum refining complexes.