An unprecedented use of plastics has caused many environmental
issues, and as usual, there is a growing interest in recycling and
reusing single-use household plastics. In this work, a mixture of
five prominent plastic polymers, as simulated household waste, was
depolymerized via the hydrothermal liquefaction (HTL) process using
a pretreated red mud catalyst (RM) for the liquid product at 430 ±
20 °C reaction temperature for an average 2 h residence time.
The selected plastics were polyethylene terephthalate (PET), high-density
polyethylene (HDPE), low-density polyethylene (LDPE), polypropylene
(PP), and polystyrene (PS), which were blended at a ratio of 42, 20,
20, 4, and 14 wt %, respectively, to form a plastic mixture (PM) as
a simulated household plastic waste. Additionally, each plastic type
was treated individually for control experiments. Among the single
plastics, HDPE generated a maximum crude oil yield of 76 wt %, whereas
PET produced mainly solid (80 wt %) and gaseous products. The crude
oil yield production from noncatalytic reactions followed this trend:
HDPE > PS > PP > LDPE. The plastic crude oil possessed 36–92
wt % gasoline-range compounds. Without a catalyst, HDPE decomposed
into straight-chain alkanes, whereas PP- and PS-derived products consisted
of cyclic compounds. The noncatalytic PM HTL reaction produced 23
wt % liquid crude product and 23 wt % solid from PET. Though the use
of a catalyst decreased the single plastic crude yield by 5–60%,
it reduced viscosity by 20–80%, minimized acidity by 14–57%,
and increased low boiling products (gasoline range) of HTL oil by
5–80%. The use of the RM catalyst increased the crude yield
of PM by 63%, decreased solid output from PET by 10%, improved energy
recovery by 4.7%, promoted aromatization in PM-derived crudes by 11.4%,
and increased the gasoline boiling range compounds by 18.3%. Additionally,
the RM catalyst was recycled without significant change in the PM
crude yield. This liquefaction study can help in mitigating plastic
recycling issues with liquid fuel production.