“…Pyrolysis of tire waste has been carried out using different reactors, including fixed bed reactors (de Marco et al, 2001), thermogravimetric analysis (Teng et al, 1998), spouted beds (Lopez et al, 2009), fluidized bed pyrolysis (Kaminsky and Mennerich, 2001), vacuum pyrolysis (Roy et al, 1995), and rotary kiln (Li et al, 2004). The primary objective of these studies was to investigate the effect of various process variables such as temperature, reaction time, feedstock size and type, and scale of the reactor on pyrolysis products and how to increase the quantity of produced liquid oil, but not the quality of liquid oil (Kraiem et al, 2016;Wu et al, 2016;Wan et al, 2014). For example, Cunliffe et al (1998) concluded that increase in temperature from 450 to 600 °C decreased the liquid oil yield from tire waste pyrolysis.…”