To investigate the yields of specific compounds and compound classes that c
an be achieved by co-processing single-stream plastic waste in carbonisatio
n, a series of Gray-King tests have been conducted on blends of Gascoigne W
ood (UK high volatile bituminous coal) and both low density polyethene (500
and 600 degrees C) and polystyrene (600 degrees C). For both polymers the
tar yields were found to increase linearly as a function of the amount of p
olymer used in the coal blend, with the actual and predicted tar yields bei
ng identical within experimental error, indicating that no synergism exists
between the coal and the polymers under the conditions used. The higher ta
r yields obtained with increasing polyethene content are accounted for by t
he increase in the concentration of aliphatics in the tars. Although little
variation was evident in the distribution of n-alkanes obtained with incre
asing polyethene content, average n-alkane/n-alkene ratios for low levels o
f polymer addition were considerably higher than predicted, indicating that
dehydrogenation of the alkanes may be taking place, with hydrogen transfer
to the coal. Furthermore, the presence of coal was found to have a signifi
cant effect on the major products derived from polystyrene. Ethylbenzene, a
s opposed to styrene monomer, was the major product from all coal/polystyre
ne blends studied, indicating that in the case of coal/polystyrene blends,
hydrogen is transferred from the coal to the polymer. A clear advantage of
using polyethene and other alkane polymers in low temperature carbonisation
processes would be the considerable reductions achieved in the viscosities
of the resultant tars which eases handling problems. Further, it was obser
ved in tests that there was no reduction in the quality of the coke (in ter
ms of Gray-King type) until 10 wt% polyethene and 2-3 wt% polystyrene had b
een added to the coal blend. (C) 1999 Elsevier Science Ltd. All rights rese
rved.