Single plastics and mixed waste plastics from different
industrial
and commercial sectors have been investigated in relation to the production
of hydrogen and syngas using a pyrolysis–catalytic steam reforming
process. The catalyst used was a carbonaceous char catalyst produced
from the pyrolysis of waste tires. Total gas yields from the processing
of single plastics were between 36.84 and 39.08 wt % (based on the
input of plastic, reacted steam, and char gasification) but those
in terms of the gas yield based only on the mass of plastic used were
very high. For example, for low-density polyethylene (LDPE) processing
at a catalyst temperature of 1000 °C, the gas yield was 445.07
wt % since both the reforming of the plastic and also the steam gasification
of the char contributed to the gas yield. The product gas was largely
composed of H2 and CO, i.e., syngas (∼80 vol %),
and the yield was significantly increased as the char catalyst temperature
was raised from 900 to 1000 °C. Hydrogen yields for the processing
of the polyolefin single plastics were ∼130 mmol gplastic
–1 at a catalyst temperature of 1000 °C. The
pyrolysis–catalytic steam reforming of the industrial and commercial
mixed plastics with the tire char catalyst produced hydrogen yields
that ranged from 92.81 to 122.6 mmol gplastic
–1 and was dependent on the compositional fraction of the individual
plastics in their mixtures. The tire char catalyst in the process
acted as both a catalyst for the steam reforming of the plastics pyrolysis
volatiles to produce hydrogen and also as a reactant (“sacrificed”),
via carbon-steam gasification to produce further hydrogen.