The rapid thermal degradation of
olefin plastics is a promising
chemical recycling technology to create useful products from waste
plastics. In this study, pyrolysis vapors from polyethylene (HDPE
and LDPE) and polypropylene were subjected to secondary degradation
using a new two-stage micropyrolysis reactor (TSMR) accessory to a
commercial micropyrolysis unit. Variations in reactor temperature
(550–600 °C) and vapor residence time (VRT) (1.4–5.6
s) showed a strong effect on the product distribution, which was comprised
of mostly alkene hydrocarbons over a broad carbon number range, with
minor production of alkanes and alkadienes. On the basis of the generated
micropyrolysis data, a very practical lumped kinetic model comprised
of 10 reactions and 6 lumped “species” was created to
describe the plastic pyrolysis and to understand how temperature and
VRT turn the product distribution into different product classes of
compounds (plastic, wax, heavy oil, light oil, gas, and aromatics).
The kinetic parameters, such as the activation energy and frequency
factor, were solved for using the method of least squares. The presented
kinetic model shows good agreement with the data and with known degradation
mechanisms.