Exploratory work was carried out to develop a process for conversion of mix
ed plastic wastes into liquid transportation fuels or petrochemicals. The c
oncept used is based on thermal depolymerization of the polymers in a suita
ble solvent followed by catalytic conversion of the resulting polymeric fra
gments into hydrocarbons with boiling points below 525 degrees C. The proce
ss is carried out batch-wise over a zeolite catalyst at temperatures from 3
50 degrees C to 450 degrees C and at atmospheric pressure. No hydrogen is u
sed and volatile products formed are continuously removed from the reactor.
Tests were carried out on polyethylene and polypropylene alone, and on mix
tures of the two. Finally, a synthetic mixture of four different plastics w
as tested. From 90% to 98% of the plastic was converted to gases or distill
able hydrocarbons. Of this yield, from 20% to 55% was gas, primarily propyl
enes and butylenes, and from 32% to 70% was a light hydrocarbon oil. Very l
ittle non-distillable coke or residue was formed. The use of mixtures did n
ot affect the high conversions obtained, but the results could only be appr
oximately predicted based on a pro-rating of results for the individual com
ponents.