This study examines catalytic ability of various zeolite materials in converting discarded tire pyrolyzed oil by employing a moderate sized pyrolysis plant for a 10 L working volume. The yield of liquid fractions from γ-Al2O3 was greater than that of HZSM-5 and HY, whereas the least amount of condensates was formed when catalyst was not present. When enhanced tire waste pyrolysis oil was analyzed using Fourier transform infrared spectroscopy with an alumina catalyst, the stretching bands corresponding to aromatic and non-aromatic compounds were visible. The results of GC-MS examinations confirm this even more. The γ-Al2O3 catalyst yielded a higher amount of liquid oil than the other two catalysts. The cyclic unsaturated fragment percentages in liquids were decreased by the catalysts used to 53.9% with HY, 59.0% with γ-Al2O3, and 62.2% with HZSM-5, which produced aromatic chemicals. Nitrogen adsorption desorption analysis revealed that γ-Al2O3 has an enhanced surface area of 635 m2/g which improved its catalytic performance. The cracked liquid oil had viscosity (10.36 cSt), values of pour and flash temperatures of -2.2 °C and 41 °C respectively, analogous to petroleum diesel. The upgraded pyrolysis oil (10%) is blended with gasoline (90%) and emission analysis was performed. Moreover, liquid oil needs post treatment (refining) for its use as energy source in transportation application. The novelty of this research is in its comparative analysis of multiple catalysts under controlled conditions using a small pilot-scale pyrolysis reactor, which provides insights into optimizing the pyrolysis process for industrial applications.