A study of pyrolysis of olive residues (cuttings and kernels) at a temperat
ure range from 300 to 600 degrees C, has been carried out. The experiments
were performed in a captive sample reactor at atmospheric pressure under he
lium. The yields of the derived gases, pyrolytic liquids and char were dete
rmined in relation to pyrolysis temperature, at heating rates of about 200
degrees C/s.
As the pyrolysis temperature was increased the percentage mass of char decr
eased whilst gas and oil products increased. The oil products increased to
a maximum Value of similar to 30 wt% of dry biomass at about 450-550 degree
s C, The major gaseous products are CO and CO2.
A simple first order kinetic model has been applied to the evolution of tot
al losses and gases. Kinetic parameters have been estimated and compared wi
th other reported similar data. (C) 2000 Elsevier Science Ltd. All rights r
eserved.