In this paper, the influences of particle size, grade and pyrolysis tempera
ture on the oil yield have been evaluated in a laboratory scale reactor. Fi
ve categories of particle sizes from two different oil shale samples were p
yrolyzed by employing a fixed bed retorting system. The reactor and the oil
shale sample were heated at a constant rate and nitrogen gas was used to p
urge the sample, continuously, in order to remove the pyrolysis products fr
om the reactor as well as to reduce secondary reactions. The liquid product
s were condensed and collected in a series of cold glass-traps and the off-
gases analysed for their hydrocarbon and non-hydrocarbon species. Subsequen
t experiments were carried out, employing a thermogravimetric analyser, usi
ng only the four smallest particle sizes under similar conditions as applie
d to the fixed bed retort. The activation energy was determined by using th
e integral method. The pyrolysis of the investigated shales was found to co
mply with first-order kinetics within the limits of experimental error. Inc
reasing the particle size resulted in a small rise in the liquid oil yield,
but simultaneously the total gaseous production was decreased. (C) 1999 El
sevier Science Ltd. All rights reserved.